[go: up one dir, main page]

WO2018181679A1 - Method for producing peptide - Google Patents

Method for producing peptide Download PDF

Info

Publication number
WO2018181679A1
WO2018181679A1 PCT/JP2018/013147 JP2018013147W WO2018181679A1 WO 2018181679 A1 WO2018181679 A1 WO 2018181679A1 JP 2018013147 W JP2018013147 W JP 2018013147W WO 2018181679 A1 WO2018181679 A1 WO 2018181679A1
Authority
WO
WIPO (PCT)
Prior art keywords
resin
trt
peptide
dmf
fmoc
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/JP2018/013147
Other languages
French (fr)
Japanese (ja)
Inventor
文俊 住野
綾香 出口
塁 小野
裕太 廣山
輝彦 神野
浩樹 森脇
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hamari Chemicals Ltd
Original Assignee
Hamari Chemicals Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hamari Chemicals Ltd filed Critical Hamari Chemicals Ltd
Priority to KR1020197029768A priority Critical patent/KR102550717B1/en
Priority to CN201880022224.9A priority patent/CN110546155B/en
Priority to US16/496,245 priority patent/US11084846B2/en
Priority to EP18775750.5A priority patent/EP3604323A4/en
Priority to JP2019510112A priority patent/JP7061606B2/en
Publication of WO2018181679A1 publication Critical patent/WO2018181679A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K1/00General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/04General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length on carriers
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K1/00General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/04General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length on carriers
    • C07K1/045General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length on carriers using devices to improve synthesis, e.g. reactors, special vessels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/96Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with openwork frames or cages
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/181Preventing generation of dust or dirt; Sieves; Filters
    • B01F35/187Preventing generation of dust or dirt; Sieves; Filters using filters in mixers, e.g. during venting
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/90Heating or cooling systems
    • B01F35/91Heating or cooling systems using gas or liquid injected into the material, e.g. using liquefied carbon dioxide or steam
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053Details of the reactor
    • B01J19/0066Stirrers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/10Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by stirrers or by rotary drums or rotary receptacles or endless belts
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07KPEPTIDES
    • C07K1/00General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14Extraction; Separation; Purification
    • C07K1/34Extraction; Separation; Purification by filtration, ultrafiltration or reverse osmosis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/90Heating or cooling systems
    • B01F2035/99Heating

Definitions

  • the present invention relates to a method for producing a peptide. More specifically, the present invention relates to a method for mass synthesis of long-chain peptides by solid phase synthesis.
  • WO2010 / 150656 pamphlet JP 2014-124540 A Japanese Patent Laying-Open No. 2015-171695 JP 2015-47540 A JP 2016-1117005 A
  • the present invention includes a novel peptide solid-phase synthesis method for synthesizing a large amount of peptide, a novel peptide solid-phase synthesis method for synthesizing a long-chain peptide with high purity, and a novel peptide solid-phase synthesis method with few side reactions.
  • the object is to provide one or more solid phase synthesis methods.
  • a method for producing a peptide characterized in that the peptide is solid-phase synthesized under stirring of a centrifugal stirring body without blades.
  • a centrifugal stirring body without blades A main body that rotates about a rotation axis; An inlet provided on the surface of the body; A discharge port provided on the surface of the main body; A flow path connecting the suction port and the discharge port, The suction port is disposed at a position closer to the rotation shaft than the discharge port,
  • the present invention relates to a novel peptide solid-phase synthesis method for synthesizing a large amount of peptide, a novel peptide solid-phase synthesis method for synthesizing a high-purity long-chain peptide, and a side reaction (for example, a fragment peptide resin cleavage reaction).
  • a side reaction for example, a fragment peptide resin cleavage reaction.
  • one or more solid phase synthesis methods can be provided among the novel peptide solid phase synthesis methods with less undesirable side chain deprotection reactions before the final coupling reaction.
  • the reaction in the solid phase synthesis method includes a protective group introduction reaction before the coupling reaction, a carboxyl group or amino group activation reaction involved in the peptide coupling reaction before the coupling reaction, a coupling reaction, and a resin cleavage. Reactions such as a deprotection reaction after a reaction, a coupling reaction, and a resin cleavage reaction are included.
  • FIG. 2 is a front view (side view) showing one embodiment of a stirring device (quoting FIG. 1 of JP-A-2015-171695, with some modifications).
  • the HPLC chromatogram of the product of Comparative Example 1 is shown.
  • the HPLC chromatogram of the product of Comparative Example 2 is shown.
  • the HPLC chromatogram of the product of Experimental Example 3 is shown.
  • the HPLC chromatogram of the acetonitrile solution of the product of Experimental example 5 is shown.
  • the HPLC chromatogram of the product of Comparative Example 3 is shown.
  • the HPLC chromatogram of the product of Experimental Example 6 (synthetic product using M-Revo after the fifth residue coupling step) is shown.
  • the HPLC chromatogram of the product of Experimental example 6 (shaking machine synthetic
  • the HPLC chromatogram of the product of Experimental Example 7 is shown.
  • the HPLC chromatogram of the product of Experimental Example 8 is shown.
  • the HPLC chromatogram of the product of Comparative Example 4 is shown.
  • the HPLC chromatogram of the product of Comparative Example 5 is shown.
  • the HPLC chromatogram of the product of Experimental Example 9 is shown.
  • the HPLC chromatogram of the product of Comparative Example 6 is shown.
  • the present invention provides a method for producing a peptide, characterized in that the peptide is solid-phase synthesized under stirring of a centrifugal stirring body having no blades.
  • Centrifugal stirring body without blades refers to, for example, a stirring body that has no blades in appearance and has a function of stirring fluid using centrifugal force.
  • the fluid preferably contains a resin, a target peptide constituent amino acid, or a combination thereof.
  • the structure of the centrifugal agitator without blades may be, for example, a rotating body that forms a flow path by connecting a suction port close to the rotation axis and a discharge port far from the rotation axis.
  • the principle of agitation is, for example, that centrifugal force acts in the flow path due to the rotation of the stirring body, fluid is discharged in the lateral direction, the vertical flow path becomes negative pressure, and a negative pressure suction flow is generated below. There may be.
  • FIG. 1 An example of the configuration of a container equipped with a centrifugal stirring body without blades is shown in FIG.
  • a centrifugal stirring body without blades When a centrifugal stirring body without blades is rotated, centrifugal force is generated at the discharge port (a), and fluid is discharged from (a) in the lateral direction. Accordingly, a suction force is generated at the suction port (b), and a tornado-like vortex flow (c) is generated.
  • the longitudinal flow path becomes negative pressure and a negative pressure suction flow is generated in the downward direction, and a “push ⁇ pull” flow is generated.
  • a pulsation (pulse) is transmitted from the centrifugal stirring body without blades to the stirring flow, and the stirring flow is spread throughout.
  • M-Revo registered trademark
  • E-REVO etc.
  • the centrifugal stirring body without blades for example, the stirring body described in WO2010 / 150656 pamphlet, Japanese Patent No. 4418019, Japanese Patent Application Laid-Open No. 2014-124540, or the like may be used. That is, the centrifugal stirring body without blades is (1) a main body that rotates about a rotation axis; An inlet provided on the surface of the body; A discharge port provided on the surface of the main body; A flow path connecting the suction port and the discharge port, The suction port is disposed at a position closer to the rotation shaft than the discharge port, The discharge port may be a rotating body for stirring (see, for example, FIGS.
  • the discharge port is disposed at a position on the outer side in the centrifugal direction from the rotation shaft with respect to the suction port.
  • the discharge port may be a stirring rotator (see, for example, FIGS.
  • a stirrer main body that rotates a cylindrical rotating member formed of a cylindrical housing whose upper end is closed by a top plate around a central axis of the cylindrical housing by a rotation drive shaft fixed to the top plate.
  • the cylindrical rotating member is A plurality of discharge openings formed in the peripheral surface of the cylindrical housing; A plurality of extrusion protruding plate portions provided so as to protrude inwardly on the inner peripheral surface of the cylindrical housing; A suction opening provided at the lower end of the cylindrical housing;
  • a stirrer main body (for example, FIGS. 4 to 6) characterized in that it is discharged from the discharge opening to the outside as an external discharge flow from the discharge opening by centrifugal force and external stirring liquid is taken into the inside as a suction flow from the suction opening. For example).
  • a container equipped with the stirring body can be used as a stirring apparatus for stirring conditions. “Installation” refers to incorporation as a part of the apparatus.
  • a stirring device Comprising a rotating body for stirring and a flow resistor disposed adjacent to each other;
  • the stirring rotating body includes: A main body that rotates about a rotation axis; An inlet provided on the surface of the body; A discharge port provided at a position on the outer surface of the main body in the centrifugal direction from the rotation shaft with respect to the suction port; A flow path connecting the suction port and the discharge port,
  • the flow resistor is A resistor body that rotates about a resistor rotation axis; A resistor inlet provided on the surface of the resistor body; A resistor discharge port provided at a position on the outer surface of the resistor main body in the centrifugal direction from the resistor rotation shaft with respect to the resistor suction port; A resistor flow path connecting the resistor suction port and the resistor discharge port,
  • the resistor body
  • a stirrer (see, for example, FIG. 7) may be used (see JP-A-2015-171695).
  • the agitator described above is useful as a reaction vessel for peptide solid phase synthesis.
  • the reaction vessel for peptide solid phase synthesis is equipped with a cylindrical vessel and a centrifugal stirring body without blades (see, for example, FIG. 1).
  • the cylindrical container may have a bottom surface and a side surface made of plastic or glass.
  • the cylindrical container may or may not have a plastic or glass lid on the top. If peptide solid-phase synthesis can be carried out in the container, the centrifugal stirring body without blades may be arranged at any position of the cylindrical container, but it may be arranged at the lower center of the cylindrical container.
  • the peptide solid phase synthesis reaction vessel preferably further includes a heat medium jacket (cover), a heat medium suction port, and a heat medium discharge port mounted on the outside of the cylindrical container (for example, see FIG. 1). reference).
  • a heat medium jacket cover
  • a heat medium suction port for example, see FIG. 1
  • a heat medium discharge port mounted on the outside of the cylindrical container (for example, see FIG. 1). reference).
  • circulating water at about 5 to 80 ° C. may be put into the heating medium jacket from the heating medium suction port, and the circulating water may be discharged from the heating medium discharge port via the circulating water jacket.
  • the peptide solid phase synthesis reaction vessel preferably further includes a glass filter.
  • the glass filter may be, for example, a crucible type, a buch funnel type, or a plate shape, and can be obtained, for example, by purchasing a commercially available product.
  • the plate diameter of the glass filter is not particularly limited and can be changed as appropriate.
  • the size of the pores of the glass filter may be smaller than the resin (solid phase carrier) used for solid phase synthesis, and may be a size capable of filtering the liquid while the resin is held on the filter.
  • the glass filter is preferably disposed above the bottom surface of the reaction vessel for peptide solid phase synthesis and / or below the centrifugal stirring body without blades (see, for example, FIG. 1).
  • the reaction vessel for peptide solid phase synthesis is preferably equipped with a cock, and can be obtained, for example, by purchasing a commercially available product.
  • the cock (stopper) is preferably arranged below the bottom surface of the reaction vessel for peptide solid phase synthesis and the glass filter (see, for example, FIG. 1).
  • reaction vessel for peptide solid phase synthesis By installing a cock (stopper), a desired amount of liquid inside the reaction vessel for peptide solid phase synthesis can be poured out at any time, so that the operation of separating the resin from the liquid such as the reaction liquid and the washing liquid can be carried out more easily.
  • the reaction vessel for peptide solid phase synthesis is more preferably equipped with a glass filter and a cock.
  • the dimensions and centrifugal force of the rotor of the centrifugal stirring body are not particularly limited and can be appropriately changed.
  • the centrifugal stirring body preferably has a plurality of (for example, 2 to 10) discharge ports on the circumference. Is indicative of the stirring capacity of the rotor, the discharge amount coefficient (opening area total ⁇ circumferential length of the discharge port) is preferably 60cm 3 ⁇ 6000 cm 3, more preferably 200cm 3 ⁇ 2000cm 3.
  • the peptide peptide may be, for example, a peptide having 5 to 150 amino acid residues, a peptide having 5 to 34, a peptide having 15 to 100, or a peptide having 10 to 80. It may be 15 to 80 peptides, 10 to 60 peptides, or 15 to 60 peptides.
  • Peptides include, for example, Abarelix, Insulin and its analogs, Endothelin, ⁇ -Endorphin Oxytocin, Calcitonin, Carperitide, Glucagon, Glucagon-like peptide-1 (GLP-1), glucagon-like peptide-2 (GLP-2), ghrelin, goserelin, cholecystokinin, sinapultide, atrial natriuretic peptide ( ANP), Secretin, Cetrorelix, Somatostatin, Degarelix, Desmopressin, Teduglutide, Teriparatide, Brain natriuretic peptide (BNP), asopressin , Parathormone, Bradykinin, Peginesatide, Lanreotide, ⁇ -Lipotropin, ⁇ -Lipotropin, Leuprorelin, Linaclotide Alternatively, it may be a peptide such as Liraglutide or a salt
  • the salt is not particularly limited as long as it is a pharmaceutically acceptable salt.
  • pharmaceutically acceptable acid addition salts for example, pharmaceutically acceptable acid addition salts, metal salts, ammonium salts, organic amine addition salts and the like can be mentioned.
  • acid addition salts inorganic acid salts such as hydrochloride, nitrate, sulfate, phosphate; oxalate, acetate, trifluoroacetate, maleate, fumarate, tartrate, citrate, lactic acid
  • organic acid salts such as salts, malates, succinates, gluconates, ascorbates, and p-toluenesulfonic acid.
  • Examples of the metal salt include alkali metal salts such as sodium salt and potassium salt; alkaline earth metal salts such as magnesium salt and calcium salt; aluminum salt and zinc salt.
  • Examples of ammonium salts include ammonium and tetramethylammonium salts.
  • Examples of organic amine addition salts include addition salts such as piperidine. Of these, acid addition salts, organic acid salts and the like are preferable, and acetates are more preferable.
  • the reaction in the solid phase synthesis method includes a protective group introduction reaction before the coupling reaction, a carboxyl group or amino group activation reaction involved in the peptide coupling reaction before the coupling reaction, a coupling reaction, a resin cleavage reaction, a cup Reactions such as a deprotection reaction after a ring reaction and a resin cleavage reaction are included.
  • DMF / 20% piperidine may be used for the de-Fmoc group (9-fluorenylmethyloxycarbonyl group) reaction.
  • Trifluoroacetic acid may be used in the de-Boc group (tertiary butoxycarbonyl group) reaction. Further, the presence or absence of an unreacted amino group may be confirmed using a ninhydrin reaction by a method such as a Kaiser test. See the Examples section for examples of solid phase synthesis methods.
  • a large amount of peptide can be synthesized.
  • the amount of peptide that can be synthesized is preferably larger than the amount of peptide synthesized using the method for producing a peptide without using a centrifugal stirring body without blades.
  • it may be 1 g or more, or 10 g or more. It may be 100 g or more, 200 g or more, or 300 g or more.
  • the peptide synthesized using the method for producing a peptide of the present invention preferably has a higher purity than a peptide synthesized using a method for producing a peptide that does not use a centrifugal stirring body without blades.
  • a preferable HPLC purity is, for example, 60% or more, 70% or more, 80% or more, or 90% or more.
  • Peptides synthesized using the peptide production method of the present invention have fewer side-reaction products such as detrityl derivatives than peptides synthesized using a peptide production method that does not use a bladeless centrifugal stirring body. It is preferable.
  • the detrityl content is preferably, for example, 5% or less, 3% or less, or 1% or less.
  • the present invention includes embodiments in which the above configurations are combined in various ways within the technical scope of the present invention as long as the effects of the present invention are exhibited.
  • pseudo-pro is pseudoproline
  • Trt is trityl group
  • HOBt 1-hydroxy-1H-benzotriazole monohydrate
  • DMF is N, N-dimethylformamide
  • DIC is diisopropylcarbodiimide
  • DIEA Is diisopropylethylamine
  • Oxyma is ethyl (hydroxyimino) cyanoacetate
  • TFA is trifluoroacetic acid
  • TIS is tri (isopropyl) silane
  • EDT is ethanedithiol
  • Cleavage mixture is acetic acid / trifluoroethanol / dichloromethane (volume ratio) 10/10/80)
  • IPE indicates isopropyl ether
  • TFE indicates 2,2,2-trifluoroethanol.
  • Fmoc-amino acid into resin (1) Cl-Trt (2-Cl) -resin (40.00 g) and Fmoc-Phe-OH (56.17 g) were added to a reaction vessel under an argon gas atmosphere. (2) Dichloroethane (400 mL) and DIEA (25.25 mL) were added. (3) Centrifugation was performed for 3 hours or more using M-Revo (registered trademark). (4) The reaction solvent was removed, and DIEA (5.05 mL), methanol (40 mL), and dichloroethane were added in a volume that allowed the whole to be stirred.
  • the HPLC purity of the B-fragment of Experimental Example 3 is 69.2%, which is equivalent to that of Comparative Examples 1 and 2, whereas the content of detrityl compound produced as a by-product is 4.79%. It was found to be less than half that of 1 and 2. That is, the solid phase synthesis method using M-Revo (registered trademark) yielded a B-fragment having a higher purity, that is, less undesirable detrityl form than the solid phase synthesis method using a stirrer.
  • M-Revo registered trademark
  • Residue 10 (Fmoc-Arg (Pbf) -OH), Residue 15 (Fmoc-Arg (Pbf) -OH), Residue 17 (Fmoc-Met-OH), Residue 21 (Fmoc-His (Trt) -OH) and the 22nd residue (Fmoc-Lys (Boc) -OH) were subjected to double coupling.
  • the 16th residue (Fmoc-Glu (tBu) -OH) was triple-coupled and the 19th residue (Fmoc-Arg (Pbf) -OH) was coupled 4 times.
  • the production method of the present invention is useful for the production of peptides.
  • it is useful for mass synthesis of long-chain peptides while suppressing side reactions.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Biophysics (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Medicinal Chemistry (AREA)
  • Molecular Biology (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Analytical Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Peptides Or Proteins (AREA)

Abstract

The present invention addresses the problem of providing a novel peptide solid-phase synthesis method for synthesizing a peptide in a large quantity. The present invention also addresses the problem of providing a novel peptide solid-phase synthesis method for synthesizing a long-chain peptide having high purity. The present invention also addresses the problem of providing a novel peptide solid-phase synthesis method which causes few side reactions. The present invention relates to a method for producing a peptide, characterized in that the peptide is solid-phase-synthesized while stirring with a centrifugal stirrer equipped with no impeller.

Description

ペプチドの製造方法Method for producing peptide

 本発明は、ペプチドの製造方法に関する。より詳細には、本発明は、固相合成法による長鎖ペプチドの大量合成方法に関する。 The present invention relates to a method for producing a peptide. More specifically, the present invention relates to a method for mass synthesis of long-chain peptides by solid phase synthesis.

 長鎖ペプチドの固相合成法において通常用いられる撹拌の手段として、振とう撹拌、窒素バブリング撹拌、スターラー撹拌等が知られている。
 一方、遠心式撹拌体は公知であり(特許文献1~4等)、リポソームの製造装置の部品として応用された例があるが(特許文献5)、遠心式撹拌体が有機合成の分野でのペプチド固相合成装置の部品として応用された例はこれまで報告されていない。
Shaking stirring, nitrogen bubbling stirring, stirrer stirring and the like are known as stirring means usually used in the solid phase synthesis method of long chain peptides.
On the other hand, centrifugal agitation bodies are known (Patent Documents 1 to 4 etc.) and there are examples applied as parts of liposome production apparatuses (Patent Document 5), but centrifugal agitation bodies are used in the field of organic synthesis. There has been no report of an example of application as a component of a peptide solid-phase synthesizer.

WO2010/150656号パンフレットWO2010 / 150656 pamphlet 特開2014-124540号公報JP 2014-124540 A 特開2015-171695号公報Japanese Patent Laying-Open No. 2015-171695 特開2015-47540号公報JP 2015-47540 A 特開2016-117005号公報JP 2016-1117005 A

 本発明は、大量のペプチドを合成する新規なペプチド固相合成法、純度の高い長鎖ペプチドを合成する新規なペプチド固相合成法、及び、副反応が少ない新規なペプチド固相合成法のうちいずれか1以上の固相合成法を提供することを目的とする。 The present invention includes a novel peptide solid-phase synthesis method for synthesizing a large amount of peptide, a novel peptide solid-phase synthesis method for synthesizing a long-chain peptide with high purity, and a novel peptide solid-phase synthesis method with few side reactions. The object is to provide one or more solid phase synthesis methods.

 本発明者らは、上記課題を解決するために鋭意研究を重ねた結果、遠心式撹拌体をペプチド固相合成法に応用することによって、純度の高い長鎖ペプチドを大量合成できることを見出し、この知見に基づいてさらに研究を進め、本発明を完成するに至った。 As a result of intensive studies to solve the above-mentioned problems, the present inventors have found that high-purity long-chain peptides can be synthesized in large quantities by applying a centrifugal stirring body to a peptide solid phase synthesis method. Based on the findings, further research has been made and the present invention has been completed.

 すなわち、本発明は以下の発明に関する。
[1]羽根のない遠心式撹拌体の撹拌下に、ペプチドを固相合成することを特徴とするペプチドの製造方法。
[2]羽根のない遠心式撹拌体が、
 回転軸を中心に回転する本体と、
前記本体の表面に設けられる吸入口と、
前記本体の表面に設けられる吐出口と、
前記吸入口と前記吐出口を繋ぐ流通路と、を備え、
前記吸入口は、前記吐出口よりも前記回転軸に近い位置に配置され、
前記吐出口は、前記吸入口よりも前記回転軸から遠心方向外側の位置に配置されることを特徴とする、撹拌用回転体である、前記[1]に記載の製造方法。
[3]羽根のない遠心式撹拌体の固相法によるペプチド合成のための使用。
[4]羽根のない遠心式撹拌体を搭載したペプチド固相合成用反応容器。
[5]グラスフィルターを備えた、前記[4]に記載のペプチド固相合成用反応容器。
That is, the present invention relates to the following inventions.
[1] A method for producing a peptide, characterized in that the peptide is solid-phase synthesized under stirring of a centrifugal stirring body without blades.
[2] A centrifugal stirring body without blades
A main body that rotates about a rotation axis;
An inlet provided on the surface of the body;
A discharge port provided on the surface of the main body;
A flow path connecting the suction port and the discharge port,
The suction port is disposed at a position closer to the rotation shaft than the discharge port,
The manufacturing method according to [1], wherein the discharge port is a stirring rotator that is disposed at a position on the outer side in the centrifugal direction from the rotation shaft than the suction port.
[3] Use of a centrifugal stirring body without a blade for peptide synthesis by a solid phase method.
[4] A reaction vessel for peptide solid phase synthesis equipped with a centrifugal stirring body without blades.
[5] The reaction vessel for peptide solid phase synthesis according to [4], comprising a glass filter.

 本発明は、大量のペプチドを合成する新規なペプチド固相合成法、純度の高い長鎖ペプチドを合成する新規なペプチド固相合成法、及び、副反応(例えば、フラグメントペプチドのレジンの切断反応における、最終カップリング反応前の好ましくない側鎖脱保護反応等)が少ない新規なペプチド固相合成法のうちいずれか1以上の固相合成法を提供することができる。
 なお、固相合成法における反応にはカップリング反応前の保護基導入反応、カップリング反応前のペプチドのカップリング反応に関与するカルボキシル基又はアミノ基の活性化反応、カップリング反応、レジンの切断反応、カップリング反応及びレジンの切断反応後の脱保護反応等の反応が含まれる。
The present invention relates to a novel peptide solid-phase synthesis method for synthesizing a large amount of peptide, a novel peptide solid-phase synthesis method for synthesizing a high-purity long-chain peptide, and a side reaction (for example, a fragment peptide resin cleavage reaction). In addition, one or more solid phase synthesis methods can be provided among the novel peptide solid phase synthesis methods with less undesirable side chain deprotection reactions before the final coupling reaction.
The reaction in the solid phase synthesis method includes a protective group introduction reaction before the coupling reaction, a carboxyl group or amino group activation reaction involved in the peptide coupling reaction before the coupling reaction, a coupling reaction, and a resin cleavage. Reactions such as a deprotection reaction after a reaction, a coupling reaction, and a resin cleavage reaction are included.

羽根のない遠心式撹拌体を搭載した容器の構成例である。It is a structural example of the container carrying the centrifugal stirring body without a blade | wing. (a)本発明の実施の形態に係る撹拌用回転体の平面図である。(b)撹拌用回転体の正面図である(特許第4418019号公報の図1を引用)。(A) It is a top view of the rotary body for stirring which concerns on embodiment of this invention. (B) It is a front view of the rotating body for stirring (citing FIG. 1 of the patent 4418019 gazette). (a)撹拌用回転体の作動を示した平面図である。(b)撹拌用回転体の作動を示した正面図である(特許第4418019号公報の図2を引用)。(A) It is the top view which showed the action | operation of the rotary body for stirring. (B) It is the front view which showed the action | operation of the rotary body for stirring (citing FIG. 2 of patent 4418019). 撹拌機本体の一態様を示す斜視図である(特開2014-124540号公報の図2を引用、一部変更あり)。It is a perspective view which shows one aspect | mode of the stirrer main body (quoting FIG. 2 of Unexamined-Japanese-Patent No. 2014-124540, and there is a part change). 撹拌機本体の一態様を示す斜視図である(特開2014-124540号公報の図4を引用、一部変更あり)。It is a perspective view which shows one aspect | mode of the main body of a stirrer (refer FIG. 4 of Unexamined-Japanese-Patent No. 2014-124540, and there exists a part change). 撹拌機本体の一態様を示す斜視図である(特開2014-124540号公報の図6を引用、一部変更あり)。It is a perspective view which shows one aspect | mode of the stirrer main body (quoting FIG. 6 of Unexamined-Japanese-Patent No. 2014-124540, and there is a part change). 撹拌装置の一態様を示す正面図(側面図)である(特開2015-171695号公報の図1を引用、一部変更あり)。FIG. 2 is a front view (side view) showing one embodiment of a stirring device (quoting FIG. 1 of JP-A-2015-171695, with some modifications). 比較例1の生成物のHPLCクロマトグラムを示す。The HPLC chromatogram of the product of Comparative Example 1 is shown. 比較例2の生成物のHPLCクロマトグラムを示す。The HPLC chromatogram of the product of Comparative Example 2 is shown. 実験例3の生成物のHPLCクロマトグラムを示す。The HPLC chromatogram of the product of Experimental Example 3 is shown. 実験例5の生成物のアセトニトリル溶液のHPLCクロマトグラムを示す。The HPLC chromatogram of the acetonitrile solution of the product of Experimental example 5 is shown. 比較例3の生成物のHPLCクロマトグラムを示す。The HPLC chromatogram of the product of Comparative Example 3 is shown. 実験例6(5残基目カップリング工程以降にM-Revoを使用した合成品)の生成物のHPLCクロマトグラムを示す。The HPLC chromatogram of the product of Experimental Example 6 (synthetic product using M-Revo after the fifth residue coupling step) is shown. 実験例6(振とう機合成品)の生成物のHPLCクロマトグラムを示す。The HPLC chromatogram of the product of Experimental example 6 (shaking machine synthetic | combination product) is shown. 実験例7の生成物のHPLCクロマトグラムを示す。The HPLC chromatogram of the product of Experimental Example 7 is shown. 実験例8の生成物のHPLCクロマトグラムを示す。The HPLC chromatogram of the product of Experimental Example 8 is shown. 比較例4の生成物のHPLCクロマトグラムを示す。The HPLC chromatogram of the product of Comparative Example 4 is shown. 比較例5の生成物のHPLCクロマトグラムを示す。The HPLC chromatogram of the product of Comparative Example 5 is shown. 実験例9の生成物のHPLCクロマトグラムを示す。The HPLC chromatogram of the product of Experimental Example 9 is shown. 比較例6の生成物のHPLCクロマトグラムを示す。The HPLC chromatogram of the product of Comparative Example 6 is shown.

 本発明は羽根のない遠心式撹拌体の撹拌下に、ペプチドを固相合成することを特徴とするペプチドの製造方法を提供する。 The present invention provides a method for producing a peptide, characterized in that the peptide is solid-phase synthesized under stirring of a centrifugal stirring body having no blades.

羽根のない遠心式撹拌体
 羽根のない遠心式撹拌体とは、例えば、外観上撹拌体自体に羽根がなく、遠心力を利用して流体を撹拌する機能を有する撹拌体のことをいう。なお、流体は、レジン若しくは目的ペプチド構成アミノ酸、又はこれらの組み合わせを含有していることが好ましい。羽根のない遠心式撹拌体の構造は、例えば回転軸に近い吸入口と回転軸から遠い吐出口が繋がって流路を形成する回転体であってもよい。撹拌の原理は、例えば、撹拌体の回転により流路内に遠心力が作用し、横方向に流体が吐出し、縦流路が負圧になり、下方に負圧吸引流が発生することであってもよい。
Centrifugal stirring body without blades A centrifugal stirring body without blades refers to, for example, a stirring body that has no blades in appearance and has a function of stirring fluid using centrifugal force. The fluid preferably contains a resin, a target peptide constituent amino acid, or a combination thereof. The structure of the centrifugal agitator without blades may be, for example, a rotating body that forms a flow path by connecting a suction port close to the rotation axis and a discharge port far from the rotation axis. The principle of agitation is, for example, that centrifugal force acts in the flow path due to the rotation of the stirring body, fluid is discharged in the lateral direction, the vertical flow path becomes negative pressure, and a negative pressure suction flow is generated below. There may be.

 羽根のない遠心式撹拌体を搭載した容器の構成例を図1に示す。羽根のない遠心式撹拌体を回転させると吐出口(a)に遠心力が発生、(a)から横方向に流体を吐出する。それに伴い、吸入口(b)に吸引力が生じ、竜巻状のうず流(c)が発生する。縦流路が負圧となって下方向に負圧吸引流が生じ、「プッシュ→プル」流が発生する。羽根のない遠心式撹拌体から撹拌流に脈動(パルス)が伝わり、撹拌流が全体に行き渡る。
 羽根のない遠心式撹拌体としては、株式会社メデック製のM-Revo(登録商標)、E-REVO等を使用することができる。
An example of the configuration of a container equipped with a centrifugal stirring body without blades is shown in FIG. When a centrifugal stirring body without blades is rotated, centrifugal force is generated at the discharge port (a), and fluid is discharged from (a) in the lateral direction. Accordingly, a suction force is generated at the suction port (b), and a tornado-like vortex flow (c) is generated. The longitudinal flow path becomes negative pressure and a negative pressure suction flow is generated in the downward direction, and a “push → pull” flow is generated. A pulsation (pulse) is transmitted from the centrifugal stirring body without blades to the stirring flow, and the stirring flow is spread throughout.
As the centrifugal stirring body without blades, M-Revo (registered trademark), E-REVO, etc., manufactured by Medec Co., Ltd. can be used.

 羽根のない遠心式撹拌体として、例えば、WO2010/150656号パンフレット、特許第4418019号公報、特開2014-124540号公報等に記載されている撹拌体を使用してもよい。
 すなわち、羽根のない遠心式撹拌体は、
(1)回転軸を中心に回転する本体と、
前記本体の表面に設けられる吸入口と、
前記本体の表面に設けられる吐出口と、
前記吸入口と前記吐出口を繋ぐ流通路と、を備え、
前記吸入口は、前記吐出口よりも前記回転軸に近い位置に配置され、
前記吐出口は、前記吸入口よりも前記回転軸から遠心方向外側の位置に配置されることを特徴とする、撹拌用回転体(例えば図2及び3をご参照)であってもよく、
(2)回転軸方向に垂直な断面が円形状に構成される本体と、
前記本体の表面に設けられる吸入口と、
前記本体の表面に設けられる吐出口と、
前記吸入口と前記吐出口を繋ぐ流通路と、を備え、
前記吸入口は、前記吐出口よりも前記回転軸に近い位置に配置され、
前記吐出口は、前記吸入口よりも前記回転軸から半径方向外側の位置に配置されることを特徴とする、撹拌用回転体(例えば図2及び3をご参照)であってもよく、又は、
(3)上端が天板によって閉塞された円筒筐体でなる円筒回転部材を、上記天板に固着された回転駆動軸によって当該円筒筐体の中心軸線を中心として回転する撹拌機本体であって、
上記円筒回転部材は、
上記円筒筐体の周面に穿設された複数の放出開口と、
上記円筒筐体の内周面に内方に突出するように設けられた複数の押出突板部と、
上記円筒筐体の下端に設けられた吸込開口と
を有し、
上記円筒回転部材は、回転した時、上記押出突板部によって、内在する撹拌液を上記中心軸線の周りに循環させる内部循環流を生起させて当該内部循環流を形成する上記撹拌液の一部を遠心力によって上記放出開口から外部放出流として放出口から外部に放出させると共に、外部の撹拌液を上記吸込開口から吸込流として内部に取り込ませることを特徴とする撹拌機本体(例えば図4~6をご参照)であってもよい。
As the centrifugal stirring body without blades, for example, the stirring body described in WO2010 / 150656 pamphlet, Japanese Patent No. 4418019, Japanese Patent Application Laid-Open No. 2014-124540, or the like may be used.
That is, the centrifugal stirring body without blades is
(1) a main body that rotates about a rotation axis;
An inlet provided on the surface of the body;
A discharge port provided on the surface of the main body;
A flow path connecting the suction port and the discharge port,
The suction port is disposed at a position closer to the rotation shaft than the discharge port,
The discharge port may be a rotating body for stirring (see, for example, FIGS. 2 and 3), characterized in that the discharge port is disposed at a position on the outer side in the centrifugal direction from the rotation shaft with respect to the suction port.
(2) a main body having a circular cross section perpendicular to the rotation axis direction;
An inlet provided on the surface of the body;
A discharge port provided on the surface of the main body;
A flow path connecting the suction port and the discharge port,
The suction port is disposed at a position closer to the rotation shaft than the discharge port,
The discharge port may be a stirring rotator (see, for example, FIGS. 2 and 3), characterized in that the discharge port is disposed at a position radially outward from the rotation shaft with respect to the suction port, or ,
(3) A stirrer main body that rotates a cylindrical rotating member formed of a cylindrical housing whose upper end is closed by a top plate around a central axis of the cylindrical housing by a rotation drive shaft fixed to the top plate. ,
The cylindrical rotating member is
A plurality of discharge openings formed in the peripheral surface of the cylindrical housing;
A plurality of extrusion protruding plate portions provided so as to protrude inwardly on the inner peripheral surface of the cylindrical housing;
A suction opening provided at the lower end of the cylindrical housing;
When the cylindrical rotating member is rotated, a part of the stirring liquid that forms the internal circulation flow is generated by causing the internal stirring flow to circulate the existing stirring liquid around the central axis line by the extrusion protruding plate portion. A stirrer main body (for example, FIGS. 4 to 6) characterized in that it is discharged from the discharge opening to the outside as an external discharge flow from the discharge opening by centrifugal force and external stirring liquid is taken into the inside as a suction flow from the suction opening. For example).

撹拌条件
 撹拌装置として、上記撹拌体を搭載した容器等を用いることができる。「搭載」とは、装置の一部として組み込むこと等をいう。
 また、撹拌装置として、
 互いに隣接して配置される撹拌用回転体および流動抵抗体を備え、
 前記撹拌用回転体は、
 回転軸を中心に回転する本体と、
 前記本体の表面に設けられる吸入口と、
 前記本体の表面において前記吸入口よりも前記回転軸から遠心方向外側の位置に設けられる吐出口と、
 前記吸入口と前記吐出口を繋ぐ流通路と、を備え、
 前記流動抵抗体は、
 抵抗体回転軸を中心に回転する抵抗体本体と、
 前記抵抗体本体の表面に設けられる抵抗体吸入口と、
 前記抵抗体本体の表面において前記抵抗体吸入口よりも前記抵抗体回転軸から遠心方向外側の位置に設けられる抵抗体吐出口と、
 前記抵抗体吸入口と前記抵抗体吐出口を繋ぐ抵抗体流通路と、を備え、
 前記抵抗体本体は、前記撹拌用回転体の前記本体とは異なる形状もしくは異なる大きさに構成される、または前記撹拌用回転体の前記本体とは異なる姿勢に配置されることを特徴とする、撹拌装置(例えば図7をご参照)を用いてもよい(特開2015-171695号公報参照)。
 上記した撹拌装置は、ペプチド固相合成用反応容器として有用である。
 また、ペプチド固相合成用反応容器は、円柱状の容器及び羽根のない遠心式撹拌体を搭載していることが好ましい(例えば図1をご参照)。円柱状の容器は、その底面及び側面がプラスチック又はガラスからなるものであってもよい。円柱状の容器は、上部にプラスチック又はガラス製の蓋があってもよくなくてもよい。ペプチド固相合成を当該容器内で行うことができれば、羽根のない遠心式撹拌体を、円柱状の容器のどの位置に配置してもよいが、円柱状の容器の中央下部に配置することが好ましい。反応物、反応液及び/又は洗浄液を円柱状の容器の上部から入れることができる。
 また、ペプチド固相合成用反応容器は、さらに熱媒体ジャケット(被覆体)、熱媒体吸入口及び熱媒体吐出口を円柱状の容器の外側に搭載していることが好ましい(例えば図1をご参照)。例えば約5~80℃程度の循環水を熱媒体吸入口から熱媒体ジャケットへ入れて、当該循環水を、循環水ジャケット経由で、熱媒体吐出口から排出してもよい。
 ペプチド固相合成用反応容器はさらにグラスフィルターを搭載していることが好ましい。グラスフィルターは、例えばルツボ型であってもよく、ブフナロート型であってもよく、板状であってもよく、例えば市販品を購入することで入手可能である。グラスフィルターの板径は、特に限定されず適宜変更可能である。グラスフィルターの細孔の大きさは、固相合成に使用するレジン(固相担体)よりも小さく、レジンをフィルター上に保持した状態で液体をろ過できる大きさであればよい。グラスフィルターは、ペプチド固相合成用反応容器の底面よりも上に、及び/又は、羽根のない遠心式撹拌体よりも下に配置されていることが好ましい(例えば図1をご参照)。グラスフィルターを搭載することにより、レジンと反応液や洗浄液等の液体の分離操作が簡便かつ迅速に実施でき、ペプチド固相合成の操作効率が向上し得る。
 ペプチド固相合成用反応容器はコック(栓)を搭載していることが好ましく、例えば市販品を購入することで入手可能である。コック(栓)は、ペプチド固相合成用反応容器の底面及びグラスフィルターよりも下側に配置されていることが好ましい(例えば図1をご参照)。コック(栓)を搭載することにより、ペプチド固相合成用反応容器内部の液体を随時所望量注ぎ出すことができることから、レジンと反応液や洗浄液等の液体の分離操作をより簡便に実施できる。
 ペプチド固相合成用反応容器は、グラスフィルター及びコック(栓)を搭載していることがさらに好ましい。
As a stirring apparatus for stirring conditions, a container equipped with the stirring body can be used. “Installation” refers to incorporation as a part of the apparatus.
As a stirring device,
Comprising a rotating body for stirring and a flow resistor disposed adjacent to each other;
The stirring rotating body includes:
A main body that rotates about a rotation axis;
An inlet provided on the surface of the body;
A discharge port provided at a position on the outer surface of the main body in the centrifugal direction from the rotation shaft with respect to the suction port;
A flow path connecting the suction port and the discharge port,
The flow resistor is
A resistor body that rotates about a resistor rotation axis;
A resistor inlet provided on the surface of the resistor body;
A resistor discharge port provided at a position on the outer surface of the resistor main body in the centrifugal direction from the resistor rotation shaft with respect to the resistor suction port;
A resistor flow path connecting the resistor suction port and the resistor discharge port,
The resistor body is configured to have a shape or a size different from that of the main body of the stirring rotator, or is arranged in a posture different from that of the main body of the stirring rotator. A stirrer (see, for example, FIG. 7) may be used (see JP-A-2015-171695).
The agitator described above is useful as a reaction vessel for peptide solid phase synthesis.
Moreover, it is preferable that the reaction vessel for peptide solid phase synthesis is equipped with a cylindrical vessel and a centrifugal stirring body without blades (see, for example, FIG. 1). The cylindrical container may have a bottom surface and a side surface made of plastic or glass. The cylindrical container may or may not have a plastic or glass lid on the top. If peptide solid-phase synthesis can be carried out in the container, the centrifugal stirring body without blades may be arranged at any position of the cylindrical container, but it may be arranged at the lower center of the cylindrical container. preferable. Reactants, reaction liquid and / or washing liquid can be put from the upper part of the cylindrical container.
Further, the peptide solid phase synthesis reaction vessel preferably further includes a heat medium jacket (cover), a heat medium suction port, and a heat medium discharge port mounted on the outside of the cylindrical container (for example, see FIG. 1). reference). For example, circulating water at about 5 to 80 ° C. may be put into the heating medium jacket from the heating medium suction port, and the circulating water may be discharged from the heating medium discharge port via the circulating water jacket.
The peptide solid phase synthesis reaction vessel preferably further includes a glass filter. The glass filter may be, for example, a crucible type, a buch funnel type, or a plate shape, and can be obtained, for example, by purchasing a commercially available product. The plate diameter of the glass filter is not particularly limited and can be changed as appropriate. The size of the pores of the glass filter may be smaller than the resin (solid phase carrier) used for solid phase synthesis, and may be a size capable of filtering the liquid while the resin is held on the filter. The glass filter is preferably disposed above the bottom surface of the reaction vessel for peptide solid phase synthesis and / or below the centrifugal stirring body without blades (see, for example, FIG. 1). By mounting the glass filter, the operation of separating the resin and the liquid such as the reaction solution and the washing solution can be carried out simply and quickly, and the operation efficiency of the peptide solid phase synthesis can be improved.
The reaction vessel for peptide solid phase synthesis is preferably equipped with a cock, and can be obtained, for example, by purchasing a commercially available product. The cock (stopper) is preferably arranged below the bottom surface of the reaction vessel for peptide solid phase synthesis and the glass filter (see, for example, FIG. 1). By installing a cock (stopper), a desired amount of liquid inside the reaction vessel for peptide solid phase synthesis can be poured out at any time, so that the operation of separating the resin from the liquid such as the reaction liquid and the washing liquid can be carried out more easily.
The reaction vessel for peptide solid phase synthesis is more preferably equipped with a glass filter and a cock.

 遠心式撹拌体のローターの寸法及び遠心力は、特に限定されず適宜変更可能である。
 遠心式撹拌体は、円周部に複数(例えば、2~10個)の吐出口を有するものが好ましい。ローターの撹拌能力の指標となる、吐出量係数(吐出口の開口面積合計×円周長)は好ましくは60cm3~6000cm3であり、より好ましくは200cm3~2000cm3である。
The dimensions and centrifugal force of the rotor of the centrifugal stirring body are not particularly limited and can be appropriately changed.
The centrifugal stirring body preferably has a plurality of (for example, 2 to 10) discharge ports on the circumference. Is indicative of the stirring capacity of the rotor, the discharge amount coefficient (opening area total × circumferential length of the discharge port) is preferably 60cm 3 ~ 6000 cm 3, more preferably 200cm 3 ~ 2000cm 3.

ペプチド
 ペプチドは、例えばアミノ酸残基数が5~150のペプチドであってもよく、5~34のペプチドであってもよく、15~100のペプチドであってもよく、10~80のペプチドであってもよく、15~80のペプチドであってもよく、10~60のペプチドであってもよく、15~60のペプチドであってもよい。
 ペプチドは、例えばアバレリクス(Abarelix)、インスリン(Insulin)及びそのアナローグ、エンドセリン(Endothelin)、β-エンドルフィン(β-Endorphin)オキシトシン(Oxytocin)、カルシトニン(Calcitonin)、カルペリチド(Carperitide)、グルカゴン(Glucagon)、グルカゴン様ペプチド-1(GLP-1)、グルカゴン様ペプチド-2(GLP-2)、グレリン(Ghrelin)、ゴセレリン(Goserelin)、コレシストキニン(Cholecystokinin)、シナプルチド(Sinapultide)、心房性ナトリウム利尿ペプチド(ANP)、セクレチン(Secretin)、セトロレリクス(Cetrorelix)、ソマトスタチン(Somatostatin)、デガレリクス(Degarelix)、デスモプレシン(Desmopressin)、テドゥグルチド(Teduglutide)、テリパラチド(Teriparatide)、脳性ナトリウム利尿ペプチド(BNP)、バソプレシン(Vasopressin)、パラトルモン(Parathormone)、ブラジキニン(Bradykinin)、ペジネサチド(Peginesatide)、ランレオチド(Lanreotide)、β-リポトロピン(β-Lipotropin)、γ-リポトロピン(γ-Lipotropin)、リュープロレリン(Leuprorelin)、リナクロチド(Linaclotide)、若しくはリラグルチド(Liraglutide)等のペプチド又はその塩等であってもよい。塩は、薬学的に許容される塩であればよく、特に限定されない。例えば、薬学的に許容される酸付加塩、金属塩、アンモニウム塩、有機アミン付加塩等が挙げられる。酸付加塩として、塩酸塩、硝酸塩、硫酸塩、リン酸塩等の無機酸塩;シュウ酸塩、酢酸塩、トリフルオロ酢酸塩、マレイン酸塩、フマル酸塩、酒石酸塩、クエン酸塩、乳酸塩、リンゴ酸塩、コハク酸塩、グルコン酸塩、アスコルビン酸塩、p-トルエンスルホン酸等の有機酸塩が挙げられる。金属塩として、ナトリウム塩、カリウム塩等のアルカリ金属塩;マグネシウム塩、カルシウム塩等のアルカリ土類金属塩;アルミニウム塩、亜鉛塩等が挙げられる。アンモニウム塩として、アンモニウム、テトラメチルアンモニウム等の塩が挙げられる。有機アミン付加塩として、ピペリジン等の付加塩が挙げられる。中でも、酸付加塩、有機酸塩等が好ましく、酢酸塩がより好ましい。
The peptide peptide may be, for example, a peptide having 5 to 150 amino acid residues, a peptide having 5 to 34, a peptide having 15 to 100, or a peptide having 10 to 80. It may be 15 to 80 peptides, 10 to 60 peptides, or 15 to 60 peptides.
Peptides include, for example, Abarelix, Insulin and its analogs, Endothelin, β-Endorphin Oxytocin, Calcitonin, Carperitide, Glucagon, Glucagon-like peptide-1 (GLP-1), glucagon-like peptide-2 (GLP-2), ghrelin, goserelin, cholecystokinin, sinapultide, atrial natriuretic peptide ( ANP), Secretin, Cetrorelix, Somatostatin, Degarelix, Desmopressin, Teduglutide, Teriparatide, Brain natriuretic peptide (BNP), asopressin , Parathormone, Bradykinin, Peginesatide, Lanreotide, β-Lipotropin, γ-Lipotropin, Leuprorelin, Linaclotide Alternatively, it may be a peptide such as Liraglutide or a salt thereof. The salt is not particularly limited as long as it is a pharmaceutically acceptable salt. For example, pharmaceutically acceptable acid addition salts, metal salts, ammonium salts, organic amine addition salts and the like can be mentioned. As acid addition salts, inorganic acid salts such as hydrochloride, nitrate, sulfate, phosphate; oxalate, acetate, trifluoroacetate, maleate, fumarate, tartrate, citrate, lactic acid Examples thereof include organic acid salts such as salts, malates, succinates, gluconates, ascorbates, and p-toluenesulfonic acid. Examples of the metal salt include alkali metal salts such as sodium salt and potassium salt; alkaline earth metal salts such as magnesium salt and calcium salt; aluminum salt and zinc salt. Examples of ammonium salts include ammonium and tetramethylammonium salts. Examples of organic amine addition salts include addition salts such as piperidine. Of these, acid addition salts, organic acid salts and the like are preferable, and acetates are more preferable.

固相合成法
 固相合成法のプロセス条件は従来十分に確立されているので、撹拌体として羽根のない遠心式撹拌体を用いること以外は特に制限されず、公知方法(例えば、メリフィールド固相合成法等)を採用することができる。固相合成法における反応はカップリング反応前の保護基導入反応、カップリング反応前のペプチドのカップリング反応に関与するカルボキシル基又はアミノ基の活性化反応、カップリング反応、レジンの切断反応、カップリング反応及びレジンの切断反応後の脱保護反応等の反応が含まれる。脱Fmoc基(9-フルオレニルメチルオキシカルボニル基)反応にはDMF/20%ピペリジンを用いてもよい。脱Boc基(ターシャリーブトキシカルボニル基)反応にはトリフルオロ酢酸を用いてもよい。また、カイザー(Kaiser)テスト等の方法によりニンヒドリン反応を利用して未反応のアミノ基の有無を確認してもよい。
 固相合成法の例については、実施例の項を参照されたい。
Since the process conditions of the solid-phase synthesis method have been well established in the past, there is no particular limitation other than using a centrifugal stirrer without a blade as the stirrer. Synthesis methods, etc.) can be employed. The reaction in the solid phase synthesis method includes a protective group introduction reaction before the coupling reaction, a carboxyl group or amino group activation reaction involved in the peptide coupling reaction before the coupling reaction, a coupling reaction, a resin cleavage reaction, a cup Reactions such as a deprotection reaction after a ring reaction and a resin cleavage reaction are included. DMF / 20% piperidine may be used for the de-Fmoc group (9-fluorenylmethyloxycarbonyl group) reaction. Trifluoroacetic acid may be used in the de-Boc group (tertiary butoxycarbonyl group) reaction. Further, the presence or absence of an unreacted amino group may be confirmed using a ninhydrin reaction by a method such as a Kaiser test.
See the Examples section for examples of solid phase synthesis methods.

効果
 本発明のペプチドの製造法によれば、例えば大量のペプチドを合成することができる。合成し得るペプチド量は、羽根のない遠心式撹拌体を用いないペプチドの製造法を用いて合成されるペプチド量よりも多いことが好ましく、例えば、1g以上であってもよく、10g以上であってもよく、100g以上であってもよく、200g以上であってもよく、また、300g以上であってもよい。
 本発明のペプチドの製造法を用いて合成されるペプチドは、羽根のない遠心式撹拌体を用いないペプチドの製造法を用いて合成されるペプチドよりも純度が高いことが好ましい。好ましいHPLC純度は例えば60%以上、70%以上、80%以上、又は90%以上等である。
 本発明のペプチドの製造法を用いて合成されるペプチドは、羽根のない遠心式撹拌体を用いないペプチドの製造法を用いて合成されるペプチドよりも脱トリチル体等の副反応生成物が少ないことが好ましい。脱トリチル体含有率は、例えば5%以下、3%以下、又は1%以下であることが好ましい。
Effect According to the method for producing a peptide of the present invention, for example, a large amount of peptide can be synthesized. The amount of peptide that can be synthesized is preferably larger than the amount of peptide synthesized using the method for producing a peptide without using a centrifugal stirring body without blades. For example, it may be 1 g or more, or 10 g or more. It may be 100 g or more, 200 g or more, or 300 g or more.
The peptide synthesized using the method for producing a peptide of the present invention preferably has a higher purity than a peptide synthesized using a method for producing a peptide that does not use a centrifugal stirring body without blades. A preferable HPLC purity is, for example, 60% or more, 70% or more, 80% or more, or 90% or more.
Peptides synthesized using the peptide production method of the present invention have fewer side-reaction products such as detrityl derivatives than peptides synthesized using a peptide production method that does not use a bladeless centrifugal stirring body. It is preferable. The detrityl content is preferably, for example, 5% or less, 3% or less, or 1% or less.

 本発明は、本発明の効果を奏する限り、本発明の技術的範囲内において、上記の構成を種々組み合わせた態様を含む。 The present invention includes embodiments in which the above configurations are combined in various ways within the technical scope of the present invention as long as the effects of the present invention are exhibited.

 次に、実施例を挙げて本発明をさらに具体的に説明するが、本発明はこれらの実施例により何ら限定されるものではなく、多くの変形が本発明の技術的思想内で当分野において通常の知識を有する者により可能である。 EXAMPLES Next, the present invention will be described more specifically with reference to examples. However, the present invention is not limited to these examples at all, and many variations are within the technical idea of the present invention. This is possible by those with ordinary knowledge.

 実施例において以下のHPLC条件で測定した。
カラム:Waters XBridge Shield18 3.5 μm 4.6×150 mm
移動相A:0.1% TFA水溶液
移動相B:0.08% TFAアセトニトリル溶液
流速:1 mL/min
検出器:UV 220 nm
In the examples, the measurement was performed under the following HPLC conditions.
Column: Waters XBridge Shield18 3.5 μm 4.6 × 150 mm
Mobile phase A: 0.1% TFA aqueous solution Mobile phase B: 0.08% TFA acetonitrile solution Flow rate: 1 mL / min
Detector: UV 220 nm

Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001

Figure JPOXMLDOC01-appb-T000002
Figure JPOXMLDOC01-appb-T000002

Figure JPOXMLDOC01-appb-T000003
Figure JPOXMLDOC01-appb-T000003

Figure JPOXMLDOC01-appb-T000004
Figure JPOXMLDOC01-appb-T000004

 本開示において、pseudo-proはシュードプロリンを、Trtはトリチル基を、HOBtは1-ヒドロキシ-1H-ベンゾトリアゾールモノハイドレートを、DMFはN,N-ジメチルホルムアミドを、DICはジイソプロピルカルボジイミドを、DIEAはジイソプロピルエチルアミンを、Oxymaはエチル(ヒドロキシイミノ)シアノアセタートを、TFAはトリフルオロ酢酸を、TISはトリ(イソプロピル)シランを、EDTはエタンジチオールを、Cleavage mixtureは酢酸/トリフルオロエタノール/ジクロロメタン(体積比10/10/80)を、IPEはイソプロピルエーテルを、TFEは2,2,2-トリフルオロエタノールを示す。 In this disclosure, pseudo-pro is pseudoproline, Trt is trityl group, HOBt is 1-hydroxy-1H-benzotriazole monohydrate, DMF is N, N-dimethylformamide, DIC is diisopropylcarbodiimide, DIEA Is diisopropylethylamine, Oxyma is ethyl (hydroxyimino) cyanoacetate, TFA is trifluoroacetic acid, TIS is tri (isopropyl) silane, EDT is ethanedithiol, and Cleavage mixture is acetic acid / trifluoroethanol / dichloromethane (volume ratio) 10/10/80), IPE indicates isopropyl ether, and TFE indicates 2,2,2-trifluoroethanol.

34残基ペプチドの固相合成
 〔実験例1〕A-フラグメント-レジン(Boc-Ser(tBu)-Val-Ser(pseudo-pro)-Glu(tBu)-Ile-Gln(Trt)-Leu-Met-His(Trt)-Asn(Trt)-Leu-Gly-O-Trt(2-Cl)-レジン)(側鎖保護型AFR-レジン)の合成(M-Revo(登録商標)を使用)
1.カップリング反応
(1)反応容器にH-Gly-O-Trt(2-Cl)-レジン(80.00 g)、Fmoc (9-Fluorenylmethoxycarbonyl)-アミノ酸(2.5 eq.)、活性化剤HOBt (22.42 g, 2.5 eq.)、反応溶媒DMF (800 mL)、DIC (25.70 mL)を添加した。
(2)M-Revo(登録商標)を使用して2時間以上遠心撹拌した。
(3)反応溶媒を除去し、M-Revo(登録商標)を使用してFmoc-アミノ酸導入レジンをDMF (800 mL)、ジクロロメタン(800 mL)、DMF (800 mL)で洗浄した。
(4)Fmoc-アミノ酸導入レジンを少量サンプリングし、カイザーテストを使用して樹脂が呈色しないことを確認した。もし、カイザーテストにより樹脂ビーズが呈色した場合は呈色しなくなるまで、操作(1)~(3)を繰り返した。
2.Fmoc基の脱保護
(5)得られたFmoc-アミノ酸導入レジンに20%ピペリジン/DMF (800 mL)を添加した。
(6)M-Revo(登録商標)を使用して20分間以上遠心撹拌した。
(7)反応溶媒を除去し、M-Revo(登録商標)を使用して(DMF 800 mL)、ジクロロメタン(800 mL)、DMF (800 mL)で洗浄した。
(8)カイザーテストにより樹脂ビーズが呈色することを確認した。
(9)操作(1)~(8)を以下の側鎖保護型AFR-レジン(230 g)が得られるまで実施した。ただし、セリン(シュードプロリン)残基は、N末端をFmoc基で保護したジペプチドであるFmoc-バリン-セリン(シュードプロリン)として導入した。
Solid-phase synthesis of 34-residue peptide [Experiment 1] A-fragment-resin (Boc-Ser (tBu) -Val-Ser (pseudo-pro) -Glu (tBu) -Ile-Gln (Trt) -Leu-Met -His (Trt) -Asn (Trt) -Leu-Gly-O-Trt (2-Cl) -resin) (side chain protected AFR-resin) synthesis (using M-Revo (registered trademark))
1. Coupling reaction (1) H-Gly-O-Trt (2-Cl) -resin (80.00 g), Fmoc (9-Fluorenylmethoxycarbonyl) -amino acid (2.5 eq.), Activator HOBt (22.42 g, 2.5 eq.), Reaction solvent DMF (800 mL), DIC (25.70 mL) were added.
(2) Centrifugation was performed for 2 hours or more using M-Revo (registered trademark).
(3) The reaction solvent was removed, and the Fmoc-amino acid introduced resin was washed with DMF (800 mL), dichloromethane (800 mL), and DMF (800 mL) using M-Revo (registered trademark).
(4) A small amount of Fmoc-amino acid-introduced resin was sampled, and it was confirmed that the resin was not colored using a Kaiser test. If the resin beads are colored by the Kaiser test, the operations (1) to (3) are repeated until no color develops.
2. Deprotection of Fmoc group (5) 20% piperidine / DMF (800 mL) was added to the obtained Fmoc-amino acid-introduced resin.
(6) The mixture was centrifuged for 20 minutes or more using M-Revo (registered trademark).
(7) The reaction solvent was removed and washed with M-Revo (registered trademark) (DMF 800 mL), dichloromethane (800 mL), DMF (800 mL).
(8) It was confirmed by the Kaiser test that the resin beads were colored.
(9) Operations (1) to (8) were carried out until the following side chain protected AFR-resin (230 g) was obtained. However, the serine (pseudoproline) residue was introduced as Fmoc-valine-serine (pseudoproline), which is a dipeptide whose N-terminus is protected with an Fmoc group.

Figure JPOXMLDOC01-appb-C000005
Figure JPOXMLDOC01-appb-C000005

〔実験例2〕B-フラグメント-レジン(H-Lys(Boc)-His(Trt)-Leu-Asn(Trt)-Ser(tBu)-Met-Glu(tBu)-Arg(Pbf)-Val-Glu(tBu)-Trp(Boc)-Leu-Arg(Pbf)-Lys(Boc)-Lys(Boc)-Leu-Gln(Trt)-Asp(tBu)-Val-His(Trt)-Asn(Trt)-Phe-O-Trt(2-Cl)-レジン)(側鎖保護型BFR-レジン)の合成(M-Revo(登録商標)を使用)
1.レジンへのFmoc-アミノ酸の導入
(1)反応容器にアルゴンガス雰囲気下でCl-Trt(2-Cl)-レジン (40.00 g)、Fmoc-Phe-OH (56.17 g)を添加した。
(2)ジクロロエタン(400 mL)及びDIEA (25.25 mL)を添加した。
(3)M-Revo(登録商標)を使用して3時間以上遠心撹拌した。
(4)反応溶媒を除去し、DIEA (5.05 mL)、メタノール (40 mL)、及びジクロロエタンを全体が撹拌可能になる容量分添加した。
(5)アルゴンガス雰囲気下でM-Revo(登録商標)を使用して1時間遠心撹拌した。
(6)反応溶媒を除去し、M-Revo(登録商標)を使用してDMF (400 mL)、ジクロロメタン(400 mL)、DMF (400 mL)で洗浄した。
(7)Fmoc-Phe-O-Trt(2-Cl)-レジンを少量サンプリングし、カイザーテストにより樹脂ビーズが呈色しないことを確認した。
2.Fmoc基の脱保護
(8)得られたFmoc-Phe-O-Trt(2-Cl)-レジンに20%ピペリジン/DMF (400 mL)を添加した。
(9)M-Revo(登録商標)を使用して20分間以上遠心撹拌した。
(10)反応溶媒を除去し、M-Revo(登録商標)を使用してDMF (400 mL)、ジクロロメタン(400 mL)、DMF (400 mL)で洗浄した。
(11)カイザーテストにより樹脂ビーズが呈色することを確認した。
(12)H-Phe-O-Trt(2-Cl)-レジンを得た。
[Experimental example 2] B-fragment-resin (H-Lys (Boc) -His (Trt) -Leu-Asn (Trt) -Ser (tBu) -Met-Glu (tBu) -Arg (Pbf) -Val-Glu (tBu) -Trp (Boc) -Leu-Arg (Pbf) -Lys (Boc) -Lys (Boc) -Leu-Gln (Trt) -Asp (tBu) -Val-His (Trt) -Asn (Trt)- Synthesis of Phe-O-Trt (2-Cl) -resin) (side chain protected BFR-resin) (using M-Revo (registered trademark))
1. Introduction of Fmoc-amino acid into resin (1) Cl-Trt (2-Cl) -resin (40.00 g) and Fmoc-Phe-OH (56.17 g) were added to a reaction vessel under an argon gas atmosphere.
(2) Dichloroethane (400 mL) and DIEA (25.25 mL) were added.
(3) Centrifugation was performed for 3 hours or more using M-Revo (registered trademark).
(4) The reaction solvent was removed, and DIEA (5.05 mL), methanol (40 mL), and dichloroethane were added in a volume that allowed the whole to be stirred.
(5) Centrifugation was performed for 1 hour using M-Revo (registered trademark) under an argon gas atmosphere.
(6) The reaction solvent was removed and washed with DMF (400 mL), dichloromethane (400 mL) and DMF (400 mL) using M-Revo (registered trademark).
(7) A small amount of Fmoc-Phe-O-Trt (2-Cl) -resin was sampled, and it was confirmed by a Kaiser test that the resin beads were not colored.
2. Deprotection of Fmoc group (8) To the obtained Fmoc-Phe-O-Trt (2-Cl) -resin, 20% piperidine / DMF (400 mL) was added.
(9) Centrifugation was performed for 20 minutes or more using M-Revo (registered trademark).
(10) The reaction solvent was removed and washed with DMF (400 mL), dichloromethane (400 mL) and DMF (400 mL) using M-Revo (registered trademark).
(11) It was confirmed by the Kaiser test that the resin beads were colored.
(12) H-Phe-O-Trt (2-Cl) -resin was obtained.

3.カップリング反応
(13)反応容器に(12)で得たH-Phe-O-Trt(2-Cl)-レジン、Fmoc-アミノ酸(2.5 eq.)、HOBt (19.59 g, 2.5 eq.)、DMF(10~20 v/w)、DIC (22.45 mL, 2.5 eq.)を添加した。
(14)M-Revo(登録商標)を使用して2時間以上遠心撹拌した。
(15)反応溶媒を除去し、M-Revo(登録商標)を使用してFmoc-アミノ酸導入レジンをDMF、ジクロロメタン、DMFで洗浄した。
(16)Fmoc-アミノ酸導入レジンを少量サンプリングし、カイザーテストにより樹脂ビーズが呈色しないことを確認した。もし、カイザーテストにより樹脂ビーズが呈色した場合は呈色しなくなるまで、操作(13)~(15)を繰り返した。
4.Fmoc基の脱保護
(17)得られたFmoc-アミノ酸導入レジンに20%ピペリジン/DMF (400 mL)を添加した。
(18)M-Revo(登録商標)を使用して20分間以上遠心撹拌した。
(19)反応溶媒を除去し、M-Revo(登録商標)を使用してDMF (400 mL)、ジクロロメタン(400 mL)、DMF (400 mL)で洗浄した。
(20)カイザーテストにより樹脂ビーズが呈色することを確認した。
(21)操作(13)~(20)を以下の側鎖保護型BFR-レジン(310 g)が得られるまで実施した。
3. Coupling reaction (13) H-Phe-O-Trt (2-Cl) -resin obtained in (12), Fmoc-amino acid (2.5 eq.), HOBt (19.59 g, 2.5 eq.), DMF (10-20 v / w), DIC (22.45 mL, 2.5 eq.) Was added.
(14) Centrifugation was performed for 2 hours or more using M-Revo (registered trademark).
(15) The reaction solvent was removed, and the Fmoc-amino acid-introduced resin was washed with DMF, dichloromethane, and DMF using M-Revo (registered trademark).
(16) A small amount of Fmoc-amino acid-introduced resin was sampled, and it was confirmed by a Kaiser test that the resin beads were not colored. If the resin beads are colored by the Kaiser test, the operations (13) to (15) are repeated until the resin beads are not colored.
4). Deprotection of Fmoc group (17) 20% piperidine / DMF (400 mL) was added to the obtained Fmoc-amino acid-introduced resin.
(18) Centrifugation was performed for 20 minutes or more using M-Revo (registered trademark).
(19) The reaction solvent was removed and washed with DMF (400 mL), dichloromethane (400 mL), and DMF (400 mL) using M-Revo (registered trademark).
(20) It was confirmed by the Kaiser test that the resin beads were colored.
(21) Operations (13) to (20) were carried out until the following side chain protected BFR-resin (310 g) was obtained.

Figure JPOXMLDOC01-appb-C000006
Figure JPOXMLDOC01-appb-C000006

〔実験例3〕側鎖保護型BFR-レジンからの保護ペプチドの切り出し(M-Revo(登録商標)を使用)
(1)側鎖保護型BFR-レジン(80 g)を添加した容器に脱気したCleavage mixture (800 mL)を添加した。
(2)M-Revo(登録商標)を使用して2時間遠心撹拌した。
(3)反応溶液をろ過し、Cleavage mixture (80 mL)で3回、さらにジクロロメタン(160 mL)で洗浄した。
(4)ろ過液を外温25℃で減圧濃縮した。
(5)濃縮残さにジクロロメタン (160 mL)を添加して結晶を溶解した。
(6)反応容器にIPE (4000 mL)を添加し、(5)の溶解液を滴下した。
(7)室温で1時間撹拌した後、結晶を減圧ろ過し、IPE (800 mL)を使用して洗浄した。
(8)室温で真空乾燥し、側鎖保護型B-フラグメント(67.95 g)を得た。
[Experimental Example 3] Cutting out protected peptide from side chain protected BFR-resin (using M-Revo (registered trademark))
(1) A degassed leakage mixture (800 mL) was added to a container to which side chain protected BFR-resin (80 g) was added.
(2) Centrifugation was performed for 2 hours using M-Revo (registered trademark).
(3) The reaction solution was filtered, washed three times with a leakage mixture (80 mL), and further washed with dichloromethane (160 mL).
(4) The filtrate was concentrated under reduced pressure at an external temperature of 25 ° C.
(5) Dichloromethane (160 mL) was added to the concentrated residue to dissolve the crystals.
(6) IPE (4000 mL) was added to the reaction vessel, and the solution (5) was added dropwise.
(7) After stirring at room temperature for 1 hour, the crystals were filtered under reduced pressure and washed using IPE (800 mL).
(8) Vacuum-dried at room temperature to obtain side chain protected B-fragment (67.95 g).

Figure JPOXMLDOC01-appb-C000007
Figure JPOXMLDOC01-appb-C000007

〔比較例1及び2〕
 M-Revo(登録商標)の代わりにスターラーを用いた以外は実験例3と同様の固相合成法により側鎖保護型B-フラグメントを得た。
[Comparative Examples 1 and 2]
Side chain protected B-fragments were obtained by the same solid phase synthesis method as in Experimental Example 3 except that a stirrer was used instead of M-Revo (registered trademark).

〔HPLC分析(比較例1及び2並びに実験例3)〕
 比較例1及び2並びに実験例3の生成物のアセトニトリル溶液のHPLC分析した結果を表5~7及び図8~10に示した。表5、6及び7は、それぞれ、比較例1、比較例2及び実験例3の生成物のアセトニトリル溶液のHPLC分析における各生成物(脱トリチル体副生成物又はB-フラグメント)の保持時間及び含有率を示す。図8、9及び10は、それぞれ、比較例1、比較例2及び実験例3の生成物のアセトニトリル溶液のHPLCクロマトグラム(グラジエントプログラムA)を示す。
[HPLC analysis (Comparative Examples 1 and 2 and Experimental Example 3)]
The results of HPLC analysis of the acetonitrile solutions of the products of Comparative Examples 1 and 2 and Experimental Example 3 are shown in Tables 5 to 7 and FIGS. Tables 5, 6 and 7 show the retention times of each product (detrityl by-product or B-fragment) in HPLC analysis of acetonitrile solutions of the products of Comparative Example 1, Comparative Example 2 and Experimental Example 3, respectively. The content rate is shown. 8, 9 and 10 show HPLC chromatograms (gradient program A) of acetonitrile solutions of the products of Comparative Example 1, Comparative Example 2 and Experimental Example 3, respectively.

Figure JPOXMLDOC01-appb-T000008
Figure JPOXMLDOC01-appb-T000008

Figure JPOXMLDOC01-appb-T000009
Figure JPOXMLDOC01-appb-T000009

Figure JPOXMLDOC01-appb-T000010
Figure JPOXMLDOC01-appb-T000010

 実験例3並びに比較例1及び2の結果を表8にまとめた。 Table 8 summarizes the results of Experimental Example 3 and Comparative Examples 1 and 2.

Figure JPOXMLDOC01-appb-T000011
Figure JPOXMLDOC01-appb-T000011

 以上の結果より、実験例3のB-フラグメントのHPLC純度は69.2%で、比較例1及び2のそれと同等であるのに対して、副生した脱トリチル体含有率は4.79%で、比較例1及び2のそれの2分の1以下であることが判明した。すなわち、M-Revo(登録商標)を用いる固相合成法により、スターラーを用いた固相合成法よりも、高純度の、すなわち、好ましくない脱トリチル体が少ないB-フラグメントが得られた。 From the above results, the HPLC purity of the B-fragment of Experimental Example 3 is 69.2%, which is equivalent to that of Comparative Examples 1 and 2, whereas the content of detrityl compound produced as a by-product is 4.79%. It was found to be less than half that of 1 and 2. That is, the solid phase synthesis method using M-Revo (registered trademark) yielded a B-fragment having a higher purity, that is, less undesirable detrityl form than the solid phase synthesis method using a stirrer.

〔実験例4〕34残基ペプチドの製造
 実験例1で得た側鎖保護型AFR-レジンを実験例3と同じ方法により処理してレジンから側鎖保護型A-フラグメントを切り出し、そのC末端カルボキシル基を活性化した後、側鎖保護型B-フラグメントを反応させて、34残基ペプチドの側鎖保護体を合成し、この側鎖保護基を脱保護して、目的ペプチドを得た。
[Experimental Example 4] Production of 34-residue peptide The side chain protected AFR-resin obtained in Experimental Example 1 was treated in the same manner as in Experimental Example 3 to excise the side chain protected A-fragment from the resin, and its C-terminus. After activating the carboxyl group, the side chain protected B-fragment was reacted to synthesize a side chain protector of a 34-residue peptide, and this side chain protective group was deprotected to obtain the target peptide.

〔実験例5〕側鎖保護型A-フラグメント-レジン(Boc-Ser(tBu)-Val-Ser(pseudo-pro)-Glu(tBu)-Ile-Gln(Trt)-Leu-Met-His(Trt)-Asn(Trt)-Leu-Gly-O-Trt(2-Cl)-レジン)(側鎖保護型AFR-レジン)の合成(M-Revo(登録商標)を使用) [Experimental Example 5] Side chain protected A-fragment-resin (Boc-Ser (tBu) -Val-Ser (pseudo-pro) -Glu (tBu) -Ile-Gln (Trt) -Leu-Met-His (Trt ) -Asn (Trt) -Leu-Gly-O-Trt (2-Cl) -resin) (side chain protected AFR-resin) (using M-Revo (registered trademark))

1.レジンへのFmoc-アミノ酸の導入
(1)ナスフラスコにFmoc-Leu-OH (2.5 eq.)、DMF、HOBt (2.5 eq.)、DIC (2.5 eq.)を加えて30分撹拌した。H-Gly-O-Trt(2-Cl)-レジン (80.00 g) を加えた反応容器に、ナスフラスコ中の反応液を添加し、M-Revo(登録商標)を用いて2時間以上撹拌させた。反応溶媒を除去し、レジンをDMF、ジクロロメタン、DMFで洗浄し、Fmoc-Leu-Gly-O-Trt(2-Cl)-レジンを得た。
1. Introduction of Fmoc-amino acid into resin (1) Fmoc-Leu-OH (2.5 eq.), DMF, HOBt (2.5 eq.), And DIC (2.5 eq.) Were added to an eggplant flask and stirred for 30 minutes. Add the reaction solution in the eggplant flask to the reaction vessel containing H-Gly-O-Trt (2-Cl) -resin (80.00 g), and stir for 2 hours or more using M-Revo (registered trademark). It was. The reaction solvent was removed, and the resin was washed with DMF, dichloromethane, and DMF to obtain Fmoc-Leu-Gly-O-Trt (2-Cl) -resin.

2.Fmoc基の脱保護
(2)Fmoc-Leu-Gly-O-Trt(2-Cl)-レジンに20%ピペリジン/DMF溶液 (10 v/w) を加えた。M-Revoを用いて20分撹拌後、反応溶媒を除去した。DMF (10 v/w×5回)、ジクロロメタン(10 v/w×5回)、DMF (10 v/w×5回) で洗浄し、H-Leu-Gly-O-Trt(2-Cl)-レジンを得た。
2. Deprotection of Fmoc group (2) A 20% piperidine / DMF solution (10 v / w) was added to Fmoc-Leu-Gly-O-Trt (2-Cl) -resin. After stirring for 20 minutes using M-Revo, the reaction solvent was removed. Wash with DMF (10 v / w x 5 times), dichloromethane (10 v / w x 5 times), DMF (10 v / w x 5 times), and H-Leu-Gly-O-Trt (2-Cl) -I got a resin.

3.カップリング反応
(3)H-Leu-Gly-O-Trt(2-Cl)-レジンに、Fmoc-Asn(Trt)-OH (2.5 eq.)、HOBt (2.5 eq.)、DIC (2.5 eq.)、DMFを撹拌可能になる容量分 (約10 v/w) 加えた。M-Revo(登録商標)を用いて2時間以上撹拌後、反応溶媒を除去した。DMF、ジクロロメタン、DMFで洗浄し、Fmoc-Asn(Trt)-Leu-Gly-O-Trt(2-Cl)-レジンを得た。
(4)Fmoc-Asn(Trt)-Leu-Gly-O-Trt(2-Cl)-レジンに20%ピペリジン/DMF溶液 (10 v/w) を加えた。M-Revo(登録商標)を用いて20分撹拌後、反応溶媒を除去した。DMF、ジクロロメタン、DMFで洗浄し、H-Asn(Trt)-Leu-Gly-O-Trt(2-Cl)-レジンを得た。
(5)以降、各Fmoc-アミノ酸の導入とFmoc基の脱保護について、(1)と(2)の操作を繰り返した。なお、Fmoc-Met-OH 導入後は、撹拌開始前に10分間以上アルゴンバブリングを実施した。 
(6)12残基目にBoc-Ser(tBu)-OH (2.5 eq.)を(2)と同様の方法でカップリングした後、反応溶媒を除去した。MeOHで洗浄し、減圧乾燥すると、側鎖保護型AFR-レジン(144.12 g)を得た。
3. Coupling reaction (3) To H-Leu-Gly-O-Trt (2-Cl) -resin, Fmoc-Asn (Trt) -OH (2.5 eq.), HOBt (2.5 eq.), DIC (2.5 eq. ), DMF was added in a volume (about 10 v / w) that allowed stirring. After stirring for 2 hours or more using M-Revo (registered trademark), the reaction solvent was removed. Washing with DMF, dichloromethane and DMF gave Fmoc-Asn (Trt) -Leu-Gly-O-Trt (2-Cl) -resin.
(4) A 20% piperidine / DMF solution (10 v / w) was added to Fmoc-Asn (Trt) -Leu-Gly-O-Trt (2-Cl) -resin. After stirring for 20 minutes using M-Revo (registered trademark), the reaction solvent was removed. Washing with DMF, dichloromethane and DMF gave H-Asn (Trt) -Leu-Gly-O-Trt (2-Cl) -resin.
(5) Thereafter, the operations of (1) and (2) were repeated for the introduction of each Fmoc-amino acid and the deprotection of the Fmoc group. After introducing Fmoc-Met-OH, argon bubbling was performed for 10 minutes or more before starting stirring.
(6) After coupling Boc-Ser (tBu) -OH (2.5 eq.) To the 12th residue in the same manner as in (2), the reaction solvent was removed. After washing with MeOH and drying under reduced pressure, side chain protected AFR-resin (144.12 g) was obtained.

4.レジンからの保護ペプチドの切り出しと純度測定
(7)(6)の操作で得られた側鎖保護型AFR-レジン(一部採取したもの約20~50 mg)に酢酸/ジクロロメタン(体積比 酢酸/ジクロロメタン =1/9)を加えて1~2時間撹拌した。反応液をアセトニトリルで希釈後、HPLC分析した。
 その結果、目的物であるA-フラグメントの純度は94.1% (tR= 27.4)であるのに対して、副生した脱トリチル体含有率は0.55% (tR= 21.5)であることが判明した(図11及び表9をご参照、グラジエントプログラムB)。
4). Cutting out the protected peptide from the resin and measuring the purity (7) Side chain protected AFR-resin obtained by the procedures of (6) (approx. 20-50 mg of a partly collected product) was added to acetic acid / dichloromethane (volume ratio acetic acid / Dichloromethane = 1/9) was added and stirred for 1-2 hours. The reaction solution was diluted with acetonitrile and analyzed by HPLC.
As a result, the purity of the target A-fragment was found to be 94.1% (t R = 27.4), whereas the content of detrityl compound produced as a by-product was found to be 0.55% (t R = 21.5). (See FIG. 11 and Table 9, Gradient program B).

Figure JPOXMLDOC01-appb-T000012
Figure JPOXMLDOC01-appb-T000012

〔比較例3〕側鎖保護型A-フラグメント-レジン(Boc-Ser(tBu)-Val-Ser(pseudo-pro)-Glu(tBu)-Ile-Gln(Trt)-Leu-Met-His(Trt)-Asn(Trt)-Leu-Gly-O-Trt(2-Cl)-レジン)(側鎖保護型AFR-レジン)の調製(全自動マイクロウェーブペプチド合成装置 (Biotage Japan社製Initiator+ Alstra)を使用) [Comparative Example 3] Side chain protected A-fragment-resin (Boc-Ser (tBu) -Val-Ser (pseudo-pro) -Glu (tBu) -Ile-Gln (Trt) -Leu-Met-His (Trt ) -Asn (Trt) -Leu-Gly-O-Trt (2-Cl) -resin) (side chain protected AFR-resin) (Fully automated microwave peptide synthesizer (Biotage Japan Initiator + Alstra)) use)

1.レジンへのFmoc-アミノ酸の導入
(1)反応容器にH-Gly-O-Trt(2-Cl)-レジン (122 mg)、DMF (4.5 mL) を加えて20分間膨潤させた。ろ過後、Fmoc-Leu-OH 0.5M DMF溶液 (0.8 mL, 0.4 mmol, 4 eq.)、DIC 0.5M DMF溶液 (0.8 mL)、HOBt 0.2M DMF溶液 (2.0 mL)を加えた。75℃で5分間マイクロウェーブ (MW) 照射して反応させた後、反応溶媒を除去した。DMF (18 mL) で洗浄し、Fmoc-Leu-Gly-O-Trt(2-Cl)-レジンを得た。
1. Introduction of Fmoc-amino acid into resin (1) H-Gly-O-Trt (2-Cl) -resin (122 mg) and DMF (4.5 mL) were added to the reaction vessel and allowed to swell for 20 minutes. After filtration, Fmoc-Leu-OH 0.5M DMF solution (0.8 mL, 0.4 mmol, 4 eq.), DIC 0.5M DMF solution (0.8 mL), and HOBt 0.2M DMF solution (2.0 mL) were added. After reacting by microwave (MW) irradiation at 75 ° C. for 5 minutes, the reaction solvent was removed. Washing with DMF (18 mL) gave Fmoc-Leu-Gly-O-Trt (2-Cl) -resin.

2.Fmoc基の脱保護
(2)Fmoc-Leu-Gly-O-Trt(2-Cl)-レジン に20%ピペリジン/DMF溶液 (4.5 mL) を加えた。3分撹拌後、反応溶媒を除去し、20%ピペリジン/DMF溶液 (4.5 mL) を加えた。10分撹拌後、反応溶媒を除去した。DMF (18 mL) で洗浄し、H-Leu-Gly-O-Trt(2-Cl)-レジンを得た。
3.カップリング反応
(3)H-Leu-Gly- O-Trt(2-Cl)-レジンにFmoc-Asn(Trt)-OH 0.5M DMF溶液 (0.8 mL)、DIC 0.5M DMF溶液 (0.8 mL)、HOBt 0.2M DMF溶液 (2.0 mL) を加えた。75℃で5分間MW照射して反応させた後、反応溶媒を除去した。DMF (18 mL) で洗浄し、Fmoc-Asn(Trt)-Leu-Gly-O-Trt(2-Cl)-レジンを得た。
2. Deprotection of Fmoc group (2) A 20% piperidine / DMF solution (4.5 mL) was added to Fmoc-Leu-Gly-O-Trt (2-Cl) -resin. After stirring for 3 minutes, the reaction solvent was removed and 20% piperidine / DMF solution (4.5 mL) was added. After stirring for 10 minutes, the reaction solvent was removed. Washing with DMF (18 mL) gave H-Leu-Gly-O-Trt (2-Cl) -resin.
3. Coupling reaction (3) F-moc-Asn (Trt) -OH 0.5M DMF solution (0.8 mL), DIC 0.5M DMF solution (0.8 mL) in H-Leu-Gly-O-Trt (2-Cl) -resin, HOBt 0.2M DMF solution (2.0 mL) was added. After reacting by MW irradiation at 75 ° C. for 5 minutes, the reaction solvent was removed. Washing with DMF (18 mL) gave Fmoc-Asn (Trt) -Leu-Gly-O-Trt (2-Cl) -resin.

(4)以降、同様に(2)及び(3)の方法に従って脱保護とFmocアミノ酸のカップリングを繰り返した (Fmoc-His(Trt)-OHのカップリングは50℃で10分間反応させた)。最後の12残基目のBoc-Ser(tBu)-OH (4.0 eq.)を(1)と同様の方法でカップリングした後、反応溶媒を除去して、MeOH (13.5 mL) で洗浄し、減圧乾燥すると、側鎖保護型AFR-レジン(350 mg)を得た。 (4) Thereafter, similarly, the deprotection and Fmoc amino acid coupling were repeated according to the methods of (2) and (3) (coupling of Fmoc-His (Trt) -OH was allowed to react at 50 ° C. for 10 minutes) . After coupling the last 12th residue of Boc-Ser (tBu) -OH (4.0 eq.) In the same manner as in (1), the reaction solvent was removed and washed with MeOH (13.5 mL) When dried under reduced pressure, side chain protected AFR-resin (350 mg) was obtained.

4.レジンからの保護ペプチドの切り出しと純度測定
(5)側鎖保護型AFR-レジン(一部採取したもの約20~50 mg)に酢酸/TFE/ジクロロメタン(体積比 酢酸/TFE/ジクロロメタン =1/1/9)を加えて2時間撹拌した。反応液をアセトニトリルで希釈後、HPLC分析した。その結果、目的物であるA-フラグメントの純度は66.1% (tR= 27.9)であるのに対して、副生した脱トリチル体含有率は7.5% (tR= 22.1)であることが判明した(図12及び表10をご参照、グラジエントプログラムB)。
4). Extraction and purity measurement of protected peptide from resin (5) Acetic acid / TFE / dichloromethane (volume ratio acetic acid / TFE / dichloromethane = 1/1) to side chain protected AFR-resin (partially collected approximately 20-50 mg) / 9) was added and stirred for 2 hours. The reaction solution was diluted with acetonitrile and analyzed by HPLC. As a result, the purity of the target A-fragment was found to be 66.1% (t R = 27.9), whereas the content of detrityl compound produced as a by-product was 7.5% (t R = 22.1). (See FIG. 12 and Table 10, Gradient program B).

Figure JPOXMLDOC01-appb-T000013
Figure JPOXMLDOC01-appb-T000013

〔実験例6〕15残基ペプチド-レジン(H-Arg(Pbf)-Val-Glu(tBu)-Trp(Boc)-Leu-Arg(Pbf)-Lys(Boc)-Lys(Boc)-Leu-Gln(Trt)-Asp(tBu)-Val-His(Trt)-Asn(Trt)-Phe-O-Trt(2-Cl)-レジン)の合成(1-4残基目の導入までは振とう機( EYELA社製高速振盪機(Cute Mixier)CM-1000型又はAs One社製高速振とう機ASCM-1)を用いて撹拌操作を行った。その後、5残基目の導入からはペプチド中間体レジンを2分割して、その半量をM-Revo(登録商標)を用いる撹拌操作により、また、もう半量を振とう機を用いる撹拌操作により合成を行った。) [Experimental Example 6] 15-residue peptide-resin (H-Arg (Pbf) -Val-Glu (tBu) -Trp (Boc) -Leu-Arg (Pbf) -Lys (Boc) -Lys (Boc) -Leu- Synthesis of Gln (Trt) -Asp (tBu) -Val-His (Trt) -Asn (Trt) -Phe-O-Trt (2-Cl) -resin) (The 用 い EYELA high-speed shaker (Cute Mixier) CM-1000 type or As One high-speed shaker ASCM-1) was used for stirring. The body resin was divided into two, and half of the amount was synthesized by a stirring operation using M-Revo (registered trademark) and the other half by a stirring operation using a shaker.

1.レジンへのFmoc-アミノ酸の導入
(1)アルゴン雰囲気下、反応容器にCl-Trt(2-Cl)-レジン (4.00 g)、Fmoc-Phe-OH (6.32 g)、DIEA (2.79 mL)、ジクロロエタン (28.0 mL) を加えた。室温にて3.5時間撹拌後、ジクロロエタン (28.0 mL)で5回洗浄した。
(2)洗浄したレジンにMeOH (4.00 mL)、DIEA (0.8mL)、ジクロロエタン (28.0 mL) を加えた。20分撹拌後、反応溶媒を除去した。DMF、ジクロロメタン、DMFで洗浄し、Fmoc-Phe-O-Trt(2-Cl)-レジンを得た。
1. Introduction of Fmoc-amino acid into resin (1) Under argon atmosphere, Cl-Trt (2-Cl) -resin (4.00 g), Fmoc-Phe-OH (6.32 g), DIEA (2.79 mL), dichloroethane in a reaction vessel (28.0 mL) was added. After stirring at room temperature for 3.5 hours, the mixture was washed 5 times with dichloroethane (28.0 mL).
(2) MeOH (4.00 mL), DIEA (0.8 mL), and dichloroethane (28.0 mL) were added to the washed resin. After stirring for 20 minutes, the reaction solvent was removed. Washing with DMF, dichloromethane and DMF gave Fmoc-Phe-O-Trt (2-Cl) -resin.

2.Fmoc基の脱保護
(3)Fmoc-Phe-O-Trt(2-Cl)-レジンに20%ピペリジン/DMF溶液 (40.0 mL, 10 v/w) を加えて20分撹拌後、反応溶媒を除去した。DMF (28.0 mL, 7 v/w×5回)、ジクロロメタン(28.0 mL, 7 v/w×5回)、DMF (28.0 mL, 7 v/w×5回) で洗浄し、H-Phe-O-Trt(2-Cl)-レジンを得た。
2. Deprotection of Fmoc group (3) Add 20% piperidine / DMF solution (40.0 mL, 10 v / w) to Fmoc-Phe-O-Trt (2-Cl) -resin and stir for 20 minutes, then remove reaction solvent did. Wash with DMF (28.0 mL, 7 v / w x 5 times), dichloromethane (28.0 mL, 7 v / w x 5 times), DMF (28.0 mL, 7 v / w x 5 times), and H-Phe-O -Trt (2-Cl) -resin was obtained.

3.カップリング反応
(4)フラスコにFmoc-Asn(Trt)-OH (9.73 g, 16.3 mmol)、HOBt (2.20 g)、DIC (2.52 mL)、DMF (40.0 mL) を加えて30分撹拌後、この溶液をH-Phe-O-Trt(2-Cl)-レジンに加えて、フラスコ内部をDMFで洗い込んで、全量を2時間撹拌後、反応溶媒を除去した。
(5)レジンをDMFで洗浄してFmoc-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンを得た。
3. Coupling reaction (4) Fmoc-Asn (Trt) -OH (9.73 g, 16.3 mmol), HOBt (2.20 g), DIC (2.52 mL), DMF (40.0 mL) were added to the flask and stirred for 30 minutes. The solution was added to H-Phe-O-Trt (2-Cl) -resin, the inside of the flask was washed with DMF, the whole was stirred for 2 hours, and then the reaction solvent was removed.
(5) The resin was washed with DMF to obtain Fmoc-Asn (Trt) -Phe-O-Trt (2-Cl) -resin.

4.Fmoc基の脱保護
(6)Fmoc-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンに20%ピペリジン/DMF溶液 (40.0 mL) を加えて20分撹拌後、反応溶媒を除去した。DMF、ジクロロメタン、DMFで洗浄し、H-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンを得た。
4). Deprotection of Fmoc group (6) Add 20% piperidine / DMF solution (40.0 mL) to Fmoc-Asn (Trt) -Phe-O-Trt (2-Cl) -resin and stir for 20 min. did. Washing with DMF, dichloromethane and DMF gave H-Asn (Trt) -Phe-O-Trt (2-Cl) -resin.

5.カップリング反応
(7)H-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンに、Fmoc-His(Trt)-OH (1.01 g)、HOBt (2.20 g)、DIC (2.52 mL)、およびDMF (撹拌可能になる容量分)を加えて2時間以上撹拌後、反応溶媒を除去した。
(8)レジンをDMF、ジクロロメタン、DMFで洗浄し、Fmoc-His(Trt)-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンを得た。
(9)以後、(4)及び(5)と同様の方法に従って脱保護とカップリングを繰り返した。
(10)15残基目のFmoc-Arg(Pbf)-OHをカップリング後、(3)と同様の方法に従ってFmoc基を脱保護した後、レジンをジクロロメタン、MeOHで洗浄し、減圧乾燥すると、15残基ペプチド-レジン(10.7 g)を得た。
5). Coupling reaction (7) H-Asn (Trt) -Phe-O-Trt (2-Cl) -resin, Fmoc-His (Trt) -OH (1.01 g), HOBt (2.20 g), DIC (2.52 mL) ), And DMF (volume that can be stirred) were added and stirred for 2 hours or longer, and then the reaction solvent was removed.
(8) The resin was washed with DMF, dichloromethane, and DMF to obtain Fmoc-His (Trt) -Asn (Trt) -Phe-O-Trt (2-Cl) -resin.
(9) Thereafter, deprotection and coupling were repeated in the same manner as in (4) and (5).
(10) After coupling Fmoc-Arg (Pbf) -OH at the 15th residue, after deprotecting the Fmoc group according to the same method as in (3), the resin was washed with dichloromethane and MeOH and dried under reduced pressure. A 15-residue peptide-resin (10.7 g) was obtained.

6.レジンからの保護ペプチドの切り出しと純度測定
(11)15残基ペプチド-レジン(約20~50 mg)の一部を採取し、それに酢酸/ジクロロメタン(体積比 酢酸/ジクロロメタン =1/1)を加えて1~2時間撹拌した。反応液をアセトニトリルで希釈後、HPLC分析した。工程の一部(5残基目カップリング工程以降)にM-Revo(登録商標)を使用した合成品の結果を表11及び図13(グラジエントプログラムA)に、振とう機合成品の結果を表12及び図14(グラジエントプログラムA)に示した。その結果から明らかなように前者は後者よりも優れたHPLC純度を示した(HPLC純度:5残基目カップリング工程以降にM-Revo(登録商標)を使用した合成品93.1%、振とう機合成品89.4%)。
6). Cleavage of protected peptide from resin and purity measurement (11) A part of 15-residue peptide-resin (about 20-50 mg) was collected, and acetic acid / dichloromethane (volume ratio acetic acid / dichloromethane = 1/1) was added to it. And stirred for 1-2 hours. The reaction solution was diluted with acetonitrile and analyzed by HPLC. Table 11 and Fig. 13 (Gradient Program A) show the results of the synthetic product using M-Revo (registered trademark) for a part of the process (after the 5th residue coupling step). The results are shown in Table 12 and FIG. 14 (gradient program A). As apparent from the results, the former showed better HPLC purity than the latter (HPLC purity: 93.1% synthetic product using M-Revo (registered trademark) after the fifth residue coupling step, shaker Synthetic product 89.4%).

Figure JPOXMLDOC01-appb-T000014
Figure JPOXMLDOC01-appb-T000014

Figure JPOXMLDOC01-appb-T000015
Figure JPOXMLDOC01-appb-T000015

〔実験例7〕16残基ペプチド-レジン(H-Glu(tBu)-Arg(Pbf)-Val-Glu(tBu)-Trp(Boc)-Leu-Arg(Pbf)-Lys(Boc)-Lys(Boc)-Leu-Gln(Trt)-Asp(tBu)-Val-His(Trt)-Asn(Trt)-Phe-O-Trt(2-Cl)-レジン)の合成(全自動マイクロウェーブペプチド合成装置 (Biotage Japan社製Initiator+ Alstra)を使用) [Experimental Example 7] 16-residue peptide-resin (H-Glu (tBu) -Arg (Pbf) -Val-Glu (tBu) -Trp (Boc) -Leu-Arg (Pbf) -Lys (Boc) -Lys ( Boc) -Leu-Gln (Trt) -Asp (tBu) -Val-His (Trt) -Asn (Trt) -Phe-O-Trt (2-Cl) -resin) (fully automated microwave peptide synthesizer) (Uses Biotage Japan Initiator + Alstra)

1.レジンへのFmoc-アミノ酸の導入
(1)反応容器にH-Phe-O-Trt(2-Cl)-レジン (179 mg)、DMF (4.5 mL) を加えて20分間膨潤させた。DMFを除去後、Fmoc-Asn(Trt)-OH 0.5M DMF溶液 (0.8 mL)、DIC 0.2M DMF溶液 (2.0 mL)、Oxyma 0.5M DMF溶液 (0.8 mL) を加えた。75℃で5分間マイクロウェーブ (MW) 照射して反応させた後、反応溶媒を除去した。DMF (18 mL) で洗浄し、Fmoc-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンを得た。
1. Introduction of Fmoc-amino acid into resin (1) H-Phe-O-Trt (2-Cl) -resin (179 mg) and DMF (4.5 mL) were added to the reaction vessel and allowed to swell for 20 minutes. After removing DMF, Fmoc-Asn (Trt) -OH 0.5M DMF solution (0.8 mL), DIC 0.2M DMF solution (2.0 mL), and Oxyma 0.5M DMF solution (0.8 mL) were added. After reacting by microwave (MW) irradiation at 75 ° C. for 5 minutes, the reaction solvent was removed. Washing with DMF (18 mL) gave Fmoc-Asn (Trt) -Phe-O-Trt (2-Cl) -resin.

2.Fmoc基の脱保護
(2)Fmoc-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンに20%ピペリジン/DMF溶液 (4.5 mL) を加えた。3分撹拌後、反応溶媒を除去し、20%ピペリジン/DMF溶液 (4.5 mL) を加えた。10分撹拌後、反応溶媒を除去し、DMF (18 mL) で洗浄して、H-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンを得た。
2. Deprotection of Fmoc group (2) A 20% piperidine / DMF solution (4.5 mL) was added to Fmoc-Asn (Trt) -Phe-O-Trt (2-Cl) -resin. After stirring for 3 minutes, the reaction solvent was removed and 20% piperidine / DMF solution (4.5 mL) was added. After stirring for 10 minutes, the reaction solvent was removed and washed with DMF (18 mL) to obtain H-Asn (Trt) -Phe-O-Trt (2-Cl) -resin.

3.カップリング反応
(3)H-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンに、Fmoc-His(Trt)-OH 0.5M DMF溶液 (0.8mL)、DIC 0.5M DMF溶液 (0.8 mL)、Oxyma 0.2M DMF溶液 (2.0 mL)を加えた。
(4)50℃で10分間MW照射して反応させた後、反応溶媒を除去した。レジンをDMF (4.5 mL×4回) で洗浄して、Fmoc-His(Trt)-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンを得た。
3. Coupling reaction (3) H-Asn (Trt) -Phe-O-Trt (2-Cl) -resin, Fmoc-His (Trt) -OH 0.5M DMF solution (0.8mL), DIC 0.5M DMF solution ( 0.8 mL) and Oxyma 0.2M DMF solution (2.0 mL) were added.
(4) After reacting by MW irradiation at 50 ° C. for 10 minutes, the reaction solvent was removed. The resin was washed with DMF (4.5 mL × 4 times) to obtain Fmoc-His (Trt) -Asn (Trt) -Phe-O-Trt (2-Cl) -resin.

(5)以後、(2)~(4)と同様の操作に従って脱保護とFmocアミノ酸のカップリングを繰り返した。(Fmoc-His(Trt)-OH以外のカップリングは75℃で5分MW照射して反応を行った)。
(6)16残基目のFmoc-Glu(tBu)-OHをカップリングし、続いてFmoc基を脱保護した後、レジンをジクロロメタン、MeOHで洗浄し、減圧乾燥すると、16残基ペプチド-レジンを得た。
4.レジンからの脱保護ペプチドの切り出しと純度測定
(7)16残基ペプチド-レジン (一部採取したもの約20 mg) にTFA/TIS/H2O/EDT(体積比 TFA/TIS/H2O/EDT = 92.5/2.5/2.5/2.5)(2 mL)を加えて2時間撹拌した。ろ過し、TFAを留去した後、酢酸エチルと水を加えて分液した。水層を分取した後、酢酸エチルを加えて洗浄した (2回)。水層を精製水で希釈後、HPLC分析した(HPLC純度63.4%)(図15及び表13をご参照、グラジエントプログラムC)。
(5) Thereafter, deprotection and Fmoc amino acid coupling were repeated according to the same procedures as in (2) to (4). (Coupling other than Fmoc-His (Trt) -OH was carried out by MW irradiation at 75 ° C. for 5 minutes).
(6) Fmoc-Glu (tBu) -OH at the 16th residue was coupled, followed by deprotection of the Fmoc group, and then the resin was washed with dichloromethane and MeOH and dried under reduced pressure. Got.
4). Cleavage of deprotected peptide from resin and purity measurement (7) 16-residue peptide-resin (partially collected approximately 20 mg) was added to TFA / TIS / H 2 O / EDT (volume ratio TFA / TIS / H 2 O /EDT=92.5/2.5/2.5/2.5) (2 mL) was added and stirred for 2 hours. After filtration and removing TFA, ethyl acetate and water were added for liquid separation. The aqueous layer was separated and washed by adding ethyl acetate (twice). The aqueous layer was diluted with purified water and analyzed by HPLC (HPLC purity 63.4%) (see FIG. 15 and Table 13, gradient program C).

Figure JPOXMLDOC01-appb-T000016
Figure JPOXMLDOC01-appb-T000016

〔実験例8〕B-フラグメント-レジン(H-Lys(Boc)-His(Trt)-Leu-Asn(Trt)-Ser(tBu)-Met-Glu(tBu)-Arg(Pbf)-Val-Glu(tBu)-Trp(Boc)-Leu-Arg(Pbf)-Lys(Boc)-Lys(Boc)-Leu-Gln(Trt)-Asp(tBu)-Val-His(Trt)-Asn(Trt)-Phe-O-Trt(2-Cl)-レジン)(側鎖保護型BFR-レジン)の合成(M-Revo(登録商標)を使用) [Experimental Example 8] B-fragment-resin (H-Lys (Boc) -His (Trt) -Leu-Asn (Trt) -Ser (tBu) -Met-Glu (tBu) -Arg (Pbf) -Val-Glu (tBu) -Trp (Boc) -Leu-Arg (Pbf) -Lys (Boc) -Lys (Boc) -Leu-Gln (Trt) -Asp (tBu) -Val-His (Trt) -Asn (Trt)- Synthesis of Phe-O-Trt (2-Cl) -resin) (side chain protected BFR-resin) (using M-Revo (registered trademark))

1.レジンへのFmoc-アミノ酸の導入
(1)アルゴン雰囲気下、反応容器にCl-Trt(2-Cl)-レジン (10.0 g)、Fmoc-Phe-OH (15.0 g)、DIEA (6.75 mL)、ジクロロエタン (100 mL) を加えた。M-Revo(登録商標)を用いて3時間以上撹拌後、反応溶媒を除去した。DIEA (1.35 mL) 、MeOH (10 mL) 、ジクロロメタン (70.0 mL)を加えて、アルゴン雰囲気下、M-Revo(登録商標)を用いて20分撹拌した。DMF、ジクロロメタン、DMFで洗浄し、Fmoc-Phe-O-Trt(2-Cl)-レジンを得た。
1. Introduction of Fmoc-amino acid into resin (1) Under argon atmosphere, Cl-Trt (2-Cl) -resin (10.0 g), Fmoc-Phe-OH (15.0 g), DIEA (6.75 mL), dichloroethane in a reaction vessel (100 mL) was added. After stirring for 3 hours or more using M-Revo (registered trademark), the reaction solvent was removed. DIEA (1.35 mL), MeOH (10 mL), and dichloromethane (70.0 mL) were added, and the mixture was stirred for 20 minutes using M-Revo (registered trademark) under an argon atmosphere. Washing with DMF, dichloromethane and DMF gave Fmoc-Phe-O-Trt (2-Cl) -resin.

2.Fmoc基の脱保護
(2)Fmoc-Phe-O-Trt(2-Cl)-レジンに20%ピペリジン/DMF溶液を撹拌可能になる容量分 (約10 v/w) 加えた。M-Revo(登録商標)を用いて20分撹拌後、反応溶媒を除去した。DMF、ジクロロメタン、DMFで洗浄し、H-Phe-O-Trt(2-Cl)-レジンを得た。
2. Deprotection of Fmoc group (2) A 20% piperidine / DMF solution was added to Fmoc-Phe-O-Trt (2-Cl) -resin in a volume (about 10 v / w) that allowed stirring. After stirring for 20 minutes using M-Revo (registered trademark), the reaction solvent was removed. Washing with DMF, dichloromethane and DMF gave H-Phe-O-Trt (2-Cl) -resin.

3.カップリング反応
(3)フラスコにFmoc-Asn(Trt)-OH (23.1 g)、HOBt (5.24 g)、DIC (6.00 mL)、DMF (70.0 mL) を加えてM-Revo(登録商標)を用いて30分以上撹拌した。
(4)(3)の溶液をH-Phe-O-Trt(2-Cl)-レジンに加えて、M-Revo(登録商標)を用いて2時間以上撹拌した。
(5)反応溶媒を除去し、レジンをDMF、ジクロロメタン、DMFで洗浄して、Fmoc-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンを得た。
(6)以後、(2)~(5)と同様の方法に従って脱保護とカップリングを繰り返した。
10残基目(Fmoc-Arg(Pbf)-OH)、15残基目(Fmoc-Arg(Pbf)-OH)、17残基目(Fmoc-Met-OH)、21残基目(Fmoc-His(Trt)-OH) 、22残基目(Fmoc-Lys(Boc)-OH) はダブルカップリングを実施した。また、16残基目(Fmoc-Glu(tBu)-OH) はトリプルカップリング、19残基目(Fmoc-Arg(Pbf)-OH) は4回カップリングを行った。
(7)22残基目のFmoc-Lys(Boc)-OHのカップリング後、(2)と同様の方法に従ってFmoc基を脱保護した後、レジンをジクロロメタン、MeOHで洗浄し、減圧乾燥すると側鎖保護型BFR-レジン(78.48 g)を得た。
4.レジンからの保護ペプチドの切り出しと純度測定
(8)側鎖保護型BFR-レジン (一部採取したもの約20 mg)に酢酸/ジクロロメタン(体積比 酢酸/ジクロロメタン =1/9)を加えて2時間撹拌した。反応液を精製水/アセトニトリルで希釈後、HPLC分析した(HPLC純度92.0%)(図16及び表14をご参照、グラジエントプログラムD)。
3. Coupling reaction (3) Add Fmoc-Asn (Trt) -OH (23.1 g), HOBt (5.24 g), DIC (6.00 mL), DMF (70.0 mL) to the flask and use M-Revo (registered trademark) And stirred for 30 minutes or longer.
(4) The solution of (3) was added to H-Phe-O-Trt (2-Cl) -resin and stirred for 2 hours or more using M-Revo (registered trademark).
(5) The reaction solvent was removed, and the resin was washed with DMF, dichloromethane, and DMF to obtain Fmoc-Asn (Trt) -Phe-O-Trt (2-Cl) -resin.
(6) Thereafter, deprotection and coupling were repeated in the same manner as in (2) to (5).
Residue 10 (Fmoc-Arg (Pbf) -OH), Residue 15 (Fmoc-Arg (Pbf) -OH), Residue 17 (Fmoc-Met-OH), Residue 21 (Fmoc-His (Trt) -OH) and the 22nd residue (Fmoc-Lys (Boc) -OH) were subjected to double coupling. The 16th residue (Fmoc-Glu (tBu) -OH) was triple-coupled and the 19th residue (Fmoc-Arg (Pbf) -OH) was coupled 4 times.
(7) After coupling Fmoc-Lys (Boc) -OH at the 22nd residue, after deprotecting the Fmoc group according to the same method as (2), the resin was washed with dichloromethane and MeOH and dried under reduced pressure. A chain-protected BFR-resin (78.48 g) was obtained.
4). Cleavage of the protected peptide from the resin and purity measurement (8) Acetic acid / dichloromethane (volume ratio of acetic acid / dichloromethane = 1/9) was added to the side chain protected BFR-resin (partially collected approximately 20 mg) for 2 hours. Stir. The reaction solution was diluted with purified water / acetonitrile and then analyzed by HPLC (HPLC purity 92.0%) (see FIG. 16 and Table 14, gradient program D).

Figure JPOXMLDOC01-appb-T000017
Figure JPOXMLDOC01-appb-T000017

〔比較例4〕B-フラグメント-レジン(H-Lys(Boc)-His(Trt)-Leu-Asn(Trt)-Ser(tBu)-Met-Glu(tBu)-Arg(Pbf)-Val-Glu(tBu)-Trp(Boc)-Leu-Arg(Pbf)-Lys(Boc)-Lys(Boc)-Leu-Gln(Trt)-Asp(tBu)-Val-His(Trt)-Asn(Trt)-Phe-O-Trt(2-Cl)-レジン)(側鎖保護型BFR-レジン)の合成(振とう機を使用) Comparative Example 4 B-fragment resin (H-Lys (Boc) -His (Trt) -Leu-Asn (Trt) -Ser (tBu) -Met-Glu (tBu) -Arg (Pbf) -Val-Glu (tBu) -Trp (Boc) -Leu-Arg (Pbf) -Lys (Boc) -Lys (Boc) -Leu-Gln (Trt) -Asp (tBu) -Val-His (Trt) -Asn (Trt)- Synthesis of Phe-O-Trt (2-Cl) -resin) (side chain protected BFR-resin) (using a shaker)

1.レジンへのFmoc-アミノ酸の導入
(1)アルゴン雰囲気下、反応容器にCl-Trt(2-Cl)-レジン (2.00 g)、Fmoc-Phe-OH (2.5 eq.)、DIEA (2.5 eq.)、ジクロロエタン (約10v/w) を加えた。振とう機を用いて3時間以上撹拌後、反応溶媒を除去した。DIEA (0.5 eq.) 、MeOH (2.0 mL) 、ジクロロメタン (20 mL) を加えて、振とう機を用いて20分撹拌した。DMF (20mL)で洗浄し、Fmoc-Phe-O-Trt(2-Cl)-レジンを得た。
1. Introduction of Fmoc-amino acid into resin (1) Under argon atmosphere, Cl-Trt (2-Cl) -resin (2.00 g), Fmoc-Phe-OH (2.5 eq.), DIEA (2.5 eq.) In a reaction vessel Dichloroethane (about 10 v / w) was added. After stirring for 3 hours or more using a shaker, the reaction solvent was removed. DIEA (0.5 eq.), MeOH (2.0 mL) and dichloromethane (20 mL) were added, and the mixture was stirred for 20 minutes using a shaker. Washing with DMF (20 mL) gave Fmoc-Phe-O-Trt (2-Cl) -resin.

2.Fmoc基の脱保護
(2)Fmoc-Phe-O-Trt(2-Cl)-レジンに20%ピペリジン/DMF溶液 (14mL)を加えた。振とう機を用いて20分撹拌後、反応溶媒を除去した。DMF、ジクロロメタン、DMFで洗浄し、H-Phe-O-Trt(2-Cl)-レジンを得た。
2. Deprotection of Fmoc group (2) A 20% piperidine / DMF solution (14 mL) was added to Fmoc-Phe-O-Trt (2-Cl) -resin. After stirring for 20 minutes using a shaker, the reaction solvent was removed. Washing with DMF, dichloromethane and DMF gave H-Phe-O-Trt (2-Cl) -resin.

3.カップリング反応
(3)フラスコにFmoc-Asn(Trt)-OH (2.5 eq.)、HOBt (2.5 eq.)、DIC (2.5 eq.)、DMF (18.0 mL) を加えて、振とう機を用いて30分以上撹拌した。
(4)(3)の溶液をH-Phe-O-Trt(2-Cl)-レジンに加えて、振とう機を用いて2時間以上撹拌し、反応溶媒を除去した。レジンをDMF (20.0 mL)で洗浄して、Fmoc-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンを得た。
(5)以後、(2)~(4)と同様の操作に従って脱保護とFmoc-アミノ酸のカップリングを繰り返した。
(6)22残基目のFmoc-Lys(Boc)-OHのカップリング後、(2)と同様の方法に従ってFmoc基を脱保護した後、レジンをMeOH (20 mL) で洗浄し、減圧乾燥すると、側鎖保護型BFR-レジン(12.18 g)を得た。
3. Coupling reaction (3) Add Fmoc-Asn (Trt) -OH (2.5 eq.), HOBt (2.5 eq.), DIC (2.5 eq.), DMF (18.0 mL) to the flask, and use a shaker. And stirred for 30 minutes or longer.
(4) The solution of (3) was added to H-Phe-O-Trt (2-Cl) -resin and stirred for 2 hours or more using a shaker to remove the reaction solvent. The resin was washed with DMF (20.0 mL) to obtain Fmoc-Asn (Trt) -Phe-O-Trt (2-Cl) -resin.
(5) Thereafter, deprotection and Fmoc-amino acid coupling were repeated according to the same procedures as in (2) to (4).
(6) After coupling Fmoc-Lys (Boc) -OH at the 22nd residue, after deprotecting the Fmoc group according to the same method as (2), the resin was washed with MeOH (20 mL) and dried under reduced pressure. Then, a side chain protected BFR-resin (12.18 g) was obtained.

4.レジンからの保護ペプチドの切り出しと純度測定
(7)側鎖保護型BFR-レジン(7.59 g) に脱気したCleavage mixture (76 mL) を添加して、アルゴン雰囲気下、振とう機を用いて2時間撹拌した。
(8)レジンをさらにCleavage mixture (38 mL)、ジクロロメタン(76 mL) で洗浄した。
(9)反応液にヘキサン(760 mL) を添加して減圧濃縮した後、ジクロロメタン(15 mL) を添加して結晶を溶解した。この溶液にIPE (380 mL) を添加して結晶を晶析させた後、加圧ろ過により結晶をろ取した。
(10)結晶を減圧乾燥させた後、得られた側鎖保護型B-フラグメントの結晶を精製水/アセトニトリルで溶解後、HPLCで測定した(HPLC純度63.8 %)。その結果、目的物であるB-フラグメントの純度は63.8% (tR= 28.4)であるのに対して、副生した脱トリチル体含有率は9.2% (tR= 24.2)であることが判明した(図17及び表15をご参照、グラジエントプログラムA)。
4). Cleavage of protected peptide from resin and purity measurement (7) Add degassed Clearage mixture (76 mL) to side chain protected BFR-resin (7.59 g) and use a shaker under argon atmosphere. Stir for hours.
(8) The resin was further washed with a clearance mixture (38 mL) and dichloromethane (76 mL).
(9) After adding hexane (760 mL) to the reaction solution and concentrating under reduced pressure, dichloromethane (15 mL) was added to dissolve the crystals. IPE (380 mL) was added to this solution to crystallize crystals, and the crystals were collected by pressure filtration.
(10) After drying the crystals under reduced pressure, the obtained side chain protected B-fragment crystals were dissolved in purified water / acetonitrile and measured by HPLC (HPLC purity 63.8%). As a result, the purity of the target B-fragment was 63.8% (t R = 28.4), whereas the content of detrityl compound produced as a by-product was found to be 9.2% (t R = 24.2). (See FIG. 17 and Table 15, Gradient program A).

Figure JPOXMLDOC01-appb-T000018
Figure JPOXMLDOC01-appb-T000018

〔比較例5〕B-フラグメント-レジン(H-Lys(Boc)-His(Trt)-Leu-Asn(Trt)-Ser(tBu)-Met-Glu(tBu)-Arg(Pbf)-Val-Glu(tBu)-Trp(Boc)-Leu-Arg(Pbf)-Lys(Boc)-Lys(Boc)-Leu-Gln(Trt)-Asp(tBu)-Val-His(Trt)-Asn(Trt)-Phe-O-Trt(2-Cl)-レジン)(側鎖保護型BFR-レジン)の合成(全自動マイクロウェーブペプチド合成装置 (Biotage Japan社製Initiator+ Alstra)を使用) [Comparative Example 5] B-fragment-resin (H-Lys (Boc) -His (Trt) -Leu-Asn (Trt) -Ser (tBu) -Met-Glu (tBu) -Arg (Pbf) -Val-Glu (tBu) -Trp (Boc) -Leu-Arg (Pbf) -Lys (Boc) -Lys (Boc) -Leu-Gln (Trt) -Asp (tBu) -Val-His (Trt) -Asn (Trt)- Phe-O-Trt (2-Cl) -resin) (side chain-protected BFR-resin) (using a fully automated microwave peptide synthesizer (Initiator + Alstra manufactured by Biotage Japan))

1.レジンへのFmoc-アミノ酸の導入
(1)反応容器にH-Phe-O-Trt(2-Cl)-レジン (118 mg)、及びDMF (4.5 mL) を加えて20分間膨潤させた。DMFを除去後、Fmoc-Asn(Trt)-OH 0.5M DMF溶液 (0.8 mL)、DIC 0.5M DMF溶液 (0.8 mL)、HOBt 0.2M DMF溶液 (2.0 mL)を加えて75℃で5分間マイクロウェーブ (MW) 照射して反応させた後、反応溶媒を除去した。レジンをDMF (18 mL) で洗浄し、Fmoc-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンを得た。
1. Introduction of Fmoc-amino acid into resin (1) H-Phe-O-Trt (2-Cl) -resin (118 mg) and DMF (4.5 mL) were added to a reaction vessel and allowed to swell for 20 minutes. After removing DMF, add Fmoc-Asn (Trt) -OH 0.5M DMF solution (0.8 mL), DIC 0.5M DMF solution (0.8 mL), HOBt 0.2M DMF solution (2.0 mL) After reacting by wave (MW) irradiation, the reaction solvent was removed. The resin was washed with DMF (18 mL) to obtain Fmoc-Asn (Trt) -Phe-O-Trt (2-Cl) -resin.

2.Fmoc基の脱保護
(2)Fmoc-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンに20%ピペリジン/DMF溶液 (4.5 mL) を加えて3分撹拌後、反応溶媒を除去した。さらに、20%ピペリジン/DMF溶液 (4.5 mL) を加えて10分撹拌後、反応溶媒を除去した。レジンをDMF (18 mL) で洗浄し、H-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンを得た。
2. Deprotection of Fmoc group (2) Add 20% piperidine / DMF solution (4.5 mL) to Fmoc-Asn (Trt) -Phe-O-Trt (2-Cl) -resin and stir for 3 min. did. Further, 20% piperidine / DMF solution (4.5 mL) was added and stirred for 10 minutes, and then the reaction solvent was removed. The resin was washed with DMF (18 mL) to obtain H-Asn (Trt) -Phe-O-Trt (2-Cl) -resin.

3.カップリング反応
(3)H-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンにFmoc-His(Trt)-OH 0.5M DMF溶液 (0.8 mL)、DIC 0.5M DMF溶液 (0.8 mL) 、HOBt 0.2M DMF溶液 (2.0 mL) を加えた。
(4)全量を50℃で10分間MW照射して反応させた後、反応溶媒を除去した。レジンをDMF (18 mL) で洗浄して、Fmoc-His(Trt)-Asn(Trt)-Phe-O-Trt(2-Cl)-レジンを得た。
(5)以後、(2)~(4)と同様の操作に従って脱保護とFmoc-アミノ酸のカップリングを繰り返した(Fmoc-His(Trt)-OH以外のカップリングは75℃で5分MW照射して反応を行った)。
(6)22残基目のFmoc-Lys(Boc)-OHのカップリング後、(2)と同様の方法に従ってFmoc基を脱保護した後、レジンをジクロロメタン、MeOHで洗浄し、減圧乾燥すると側鎖保護型BFR-レジンを得た。
4.レジンからの保護ペプチドの切り出しと純度測定
(7)側鎖保護型BFR-レジン (一部採取したもの約20 mg) にCleavage mixture (2 mL) を加えて2時間撹拌した。反応液をアセトニトリルで希釈後、HPLC分析した。その結果、目的物であるB-フラグメントの純度は75.5% (tR= 20.4)であるのに対して、副生した脱トリチル体含有率は7.9% (tR= 7.9)であることが判明した(図18及び表16をご参照、グラジエントプログラムD)。
3. Coupling reaction (3) Fmoc-His (Trt) -OH 0.5M DMF solution (0.8 mL), DIC 0.5M DMF solution (0.8 mL) in H-Asn (Trt) -Phe-O-Trt (2-Cl) -resin mL) and HOBt 0.2M DMF solution (2.0 mL).
(4) The whole amount was reacted by MW irradiation at 50 ° C. for 10 minutes, and then the reaction solvent was removed. The resin was washed with DMF (18 mL) to obtain Fmoc-His (Trt) -Asn (Trt) -Phe-O-Trt (2-Cl) -resin.
(5) Thereafter, deprotection and Fmoc-amino acid coupling were repeated following the same procedures as in (2) to (4) (Coupling other than Fmoc-His (Trt) -OH was irradiated with MW for 5 minutes at 75 ° C. Reaction).
(6) After coupling Fmoc-Lys (Boc) -OH at the 22nd residue, after deprotecting the Fmoc group according to the same method as (2), the resin was washed with dichloromethane and MeOH and dried under reduced pressure. A chain-protected BFR-resin was obtained.
4). Cleavage of the protected peptide from the resin and measurement of purity (7) A clearance mixture (2 mL) was added to a side chain protected BFR-resin (approximately 20 mg of a partially collected product) and stirred for 2 hours. The reaction solution was diluted with acetonitrile and analyzed by HPLC. As a result, the purity of the target B-fragment was found to be 75.5% (t R = 20.4), whereas the content of detrityl compound produced as a by-product was 7.9% (t R = 7.9). (See FIG. 18 and Table 16, Gradient program D).

Figure JPOXMLDOC01-appb-T000019
Figure JPOXMLDOC01-appb-T000019

 実験例5~8及び比較例3~5の結果を表17にまとめた。 The results of Experimental Examples 5 to 8 and Comparative Examples 3 to 5 are summarized in Table 17.

Figure JPOXMLDOC01-appb-T000020
Figure JPOXMLDOC01-appb-T000020

 上記結果から、本発明の製造方法により高純度の長鎖ペプチドが大量に得られたことが確認できた。また、本発明の製造方法により、ペプチド固相合成法における中間体フラグメント脱トリチル体の生成が低減されることが確認できた。すなわち、本発明の製造方法により、副反応が抑制され、純度の高い長鎖ペプチドが大量合成できることが確認された。 From the above results, it was confirmed that a large amount of highly purified long-chain peptide was obtained by the production method of the present invention. Moreover, it has confirmed that the production | generation of the intermediate fragment detrityl body in the peptide solid-phase synthesis method was reduced by the manufacturing method of this invention. That is, it was confirmed that the production method of the present invention can suppress a side reaction and can synthesize a large amount of a long-chain peptide with high purity.

〔実験例9〕ペンタアラニン(H-Ala-Ala-Ala-Ala-Ala-OH)の合成(M-Revo(登録商標)を使用)
1.レジンへのFmoc-アミノ酸の導入
(1)反応容器にWang レジン (パラメトキシベンジルアルコールレジン、5.0 g)、DMF (35 mL) を添加してレジンを膨潤させた。DMFを除去後、Fmoc-Ala-OH 2.41 g(2.5 eq.)、HOBt (1.05 g, 2.5 eq.)、DMF (35 mL)、DIC (1.2 mL, 2.5 eq.)を添加した。
(2)M-Revo(登録商標)を使用して、2時間以上遠心撹拌した。
(3)反応溶媒を除去し、M-Revo(登録商標)を使用して、Fmoc-Ala-OH導入レジンをDMF (35 mL)、ジクロロメタン (35 mL)、DMF (35 mL) で洗浄した。
2.Fmoc基の脱保護
(4)得られたFmoc-Ala-Wang-レジンに20%ピペリジン/ DMF (35 mL) を添加した。
(5)M-Revo(登録商標)を使用して、20分間以上遠心撹拌した。
(6)反応溶媒を除去し、M-Revo(登録商標)を使用して、DMF (35 mL)、ジクロロメタン (35 mL)、DMF (35 mL) で洗浄した。
(7)カイザーテストにより樹脂ビーズが呈色することを確認した。
(8)H-Ala-Wang-レジンを得た。
[Experimental Example 9] Synthesis of pentaalanine (H-Ala-Ala-Ala-Ala-Ala-OH) (using M-Revo (registered trademark))
1. Introduction of Fmoc-amino acid into resin (1) Wang resin (paramethoxybenzyl alcohol resin, 5.0 g) and DMF (35 mL) were added to a reaction vessel to swell the resin. After removing DMF, Fmoc-Ala-OH 2.41 g (2.5 eq.), HOBt (1.05 g, 2.5 eq.), DMF (35 mL), and DIC (1.2 mL, 2.5 eq.) Were added.
(2) Using M-Revo (registered trademark), the mixture was centrifuged for 2 hours or more.
(3) The reaction solvent was removed, and the Fmoc-Ala-OH introduced resin was washed with DMF (35 mL), dichloromethane (35 mL), and DMF (35 mL) using M-Revo (registered trademark).
2. Deprotection of Fmoc group (4) 20% piperidine / DMF (35 mL) was added to the obtained Fmoc-Ala-Wang-resin.
(5) Using M-Revo (registered trademark), the mixture was centrifuged for 20 minutes or more.
(6) The reaction solvent was removed and washed with DMF (35 mL), dichloromethane (35 mL), and DMF (35 mL) using M-Revo (registered trademark).
(7) It was confirmed by the Kaiser test that the resin beads were colored.
(8) H-Ala-Wang-resin was obtained.

3.カップリング反応
(9)(8)の反応容器にFmoc-Ala-OH (2.41 g, 2.5 eq.)、HOBt (1.05 g, 2.5 eq.)、DMF (35 mL)、DIC (1.2 mL, 2.5 eq.)を添加した。
(10)M-Revo(登録商標)を使用して、1時間以上遠心撹拌した。
(11)反応溶媒を除去し、M-Revo(登録商標)を使用して、Fmoc-Ala-OH導入レジンをDMF (35 mL)、ジクロロメタン(35 mL)、DMF (35 mL)で洗浄した。
(12)Fmoc-Ala-OH導入レジンを少量サンプリングし、カイザーテストにより樹脂ビーズが呈色しないことを確認した。もし、カイザーテストにより樹脂ビーズが呈色した場合は呈色しなくなるまで、操作(9)~(11)を繰り返した。
(13)操作(4)~(12)をBoc-Ala-Ala-Ala-Ala-Ala-Wang-レジンが得られるまで実施した。ただし、N末端アミノ酸はBoc-Ala-OHを導入した。
(14)Boc-Ala-OHのカップリング後、ジクロロメタン(35 mL)、MeOH (35 mL)で洗浄し、減圧乾燥し、以下のBoc-Ala-Ala-Ala-Ala-Ala-Wang-レジンを得た。
3. Fmoc-Ala-OH (2.41 g, 2.5 eq.), HOBt (1.05 g, 2.5 eq.), DMF (35 mL), DIC (1.2 mL, 2.5 eq) were added to the reaction vessel for the coupling reaction (9) (8). .) Was added.
(10) Using M-Revo (registered trademark), the mixture was centrifuged for 1 hour or more.
(11) The reaction solvent was removed, and the Fmoc-Ala-OH introduced resin was washed with DMF (35 mL), dichloromethane (35 mL), and DMF (35 mL) using M-Revo (registered trademark).
(12) A small amount of Fmoc-Ala-OH introduced resin was sampled, and it was confirmed by a Kaiser test that the resin beads were not colored. If the resin beads are colored by the Kaiser test, the operations (9) to (11) are repeated until the resin beads are not colored.
(13) Operations (4) to (12) were performed until Boc-Ala-Ala-Ala-Ala-Ala-Wang-resin was obtained. However, Boc-Ala-OH was introduced as the N-terminal amino acid.
(14) After coupling Boc-Ala-OH, wash with dichloromethane (35 mL) and MeOH (35 mL), dry under reduced pressure, and add the following Boc-Ala-Ala-Ala-Ala-Ala-Wang-resin Obtained.

Figure JPOXMLDOC01-appb-C000021
Figure JPOXMLDOC01-appb-C000021

4.レジンからのペプチドの切り出し
(15)Boc-Ala-Ala-Ala-Ala-Ala-Wang-レジンにTFA/TIS/H2O(体積比TFA/TIS/H2O=95/2.5/2.5)(35 mL)を加えて2時間振とうした。
(16)反応液を減圧濃縮し、IPE (250 mL)にて晶析させた。
(17)結晶を減圧ろ過した。
(18)室温で減圧乾燥し、以下のH-Ala-Ala-Ala-Ala-Ala-OH・TFA塩(604 mg)を得た。
4). Excision of peptide from resin (15) Boc-Ala-Ala-Ala-Ala-Ala-Wang-resin with TFA / TIS / H 2 O (volume ratio TFA / TIS / H 2 O = 95 / 2.5 / 2.5) ( 35 mL) was added and shaken for 2 hours.
(16) The reaction solution was concentrated under reduced pressure and crystallized with IPE (250 mL).
(17) The crystals were filtered under reduced pressure.
(18) It dried under reduced pressure at room temperature and obtained the following H-Ala-Ala-Ala-Ala-Ala-OH.TFA salt (604 mg).

Figure JPOXMLDOC01-appb-C000022
Figure JPOXMLDOC01-appb-C000022

〔比較例6〕ペンタアラニン(H-Ala-Ala-Ala-Ala-Ala-OH)の合成(振とう機を使用)
1.レジンへのFmoc-アミノ酸の導入
(1)反応容器にWang-レジン (0.50 g)、DMF (5 mL)を添加してレジンを膨潤させた。DMFを除去後、Fmoc-Ala-OH (775 mg, 6 eq.)、HOBt (337 mg, 6 eq.)、DMF (2.5 mL)、DIC (386 μL, 6 eq.)を添加した。
(2)振とう機を使用して、2時間以上振とうした。
(3)反応溶媒を除去し、振とう機を使用して、Fmoc-Ala-OH導入レジンをDMF (5 mL)、ジクロロメタン (5 mL)、DMF (5 mL)で洗浄した。
[Comparative Example 6] Synthesis of pentaalanine (H-Ala-Ala-Ala-Ala-Ala-OH) (using a shaker)
1. Introduction of Fmoc-amino acid into resin (1) Wang-resin (0.50 g) and DMF (5 mL) were added to a reaction vessel to swell the resin. After removing DMF, Fmoc-Ala-OH (775 mg, 6 eq.), HOBt (337 mg, 6 eq.), DMF (2.5 mL), and DIC (386 μL, 6 eq.) Were added.
(2) Shake for more than 2 hours using a shaker.
(3) The reaction solvent was removed, and the Fmoc-Ala-OH introduced resin was washed with DMF (5 mL), dichloromethane (5 mL), and DMF (5 mL) using a shaker.

2.Fmoc基の脱保護
(4)得られたFmoc-Ala-Wang-レジンに20%ピペリジン/ DMF (5.5 mL)を添加した。
(5)振とう機を使用して、20分間以上振とうした。
(6)反応溶媒を除去し、振とう機を使用して、DMF (5 mL)、ジクロロメタン (5 mL)、DMF (5 mL)で洗浄した。
(7)カイザーテストにより樹脂ビーズが呈色することを確認した。
(8)H-Ala-Wang-レジンを得た。
2. Deprotection of Fmoc group (4) 20% piperidine / DMF (5.5 mL) was added to the resulting Fmoc-Ala-Wang-resin.
(5) Using a shaker, shake for 20 minutes or more.
(6) The reaction solvent was removed, and the mixture was washed with DMF (5 mL), dichloromethane (5 mL), and DMF (5 mL) using a shaker.
(7) It was confirmed by the Kaiser test that the resin beads were colored.
(8) H-Ala-Wang-resin was obtained.

3.カップリング反応
(9)(8)の反応容器にFmoc-Ala-OH (386 mg, 2.5 eq.)、HOBt (168 mg, 2.5 eq.)、DMF (5.5 mL)、DIC (206 μL, 2.5 eq.)を添加した。
(10)振とう機を使用して、1時間以上振とうした。
(11)反応溶媒を除去し、振とう機を使用して、Fmoc-Ala-OH導入レジンをDMF (5 mL)、ジクロロメタン (5 mL)、DMF (5 mL)で洗浄した。
(12)Fmoc-Ala-OH導入レジンを少量サンプリングし、カイザーテストにより樹脂ビーズが呈色しないことを確認した。もし、カイザーテストにより樹脂ビーズが呈色した場合は呈色しなくなるまで、操作(9)~(11)を繰り返した。
(13)操作(4)~(12)をBoc-Ala-Ala-Ala-Ala-Ala-Wang-レジンが得られるまで実施した。ただし、最後のカップリング反応に使用する保護アミノ酸(N末端アミノ酸)にはBoc-Ala-OHを使用した。
(14)Boc-Ala-OHのカップリング後、ジクロロメタン (5 mL)、MeOH (5 mL)で洗浄し、減圧乾燥するとBoc-Ala-Ala-Ala-Ala-Ala-Wang-レジン (0.68 g)を得た。
3. Fmoc-Ala-OH (386 mg, 2.5 eq.), HOBt (168 mg, 2.5 eq.), DMF (5.5 mL), DIC (206 μL, 2.5 eq) were added to the reaction vessel for the coupling reaction (9) (8). .) Was added.
(10) Using a shaker, shake for 1 hour or more.
(11) The reaction solvent was removed, and the Fmoc-Ala-OH introduced resin was washed with DMF (5 mL), dichloromethane (5 mL), and DMF (5 mL) using a shaker.
(12) A small amount of Fmoc-Ala-OH introduced resin was sampled, and it was confirmed by a Kaiser test that the resin beads were not colored. If the resin beads are colored by the Kaiser test, the operations (9) to (11) are repeated until the resin beads are not colored.
(13) Operations (4) to (12) were performed until Boc-Ala-Ala-Ala-Ala-Ala-Wang-resin was obtained. However, Boc-Ala-OH was used as the protected amino acid (N-terminal amino acid) used in the final coupling reaction.
(14) After coupling with Boc-Ala-OH, washed with dichloromethane (5 mL), MeOH (5 mL), and dried under reduced pressure. Boc-Ala-Ala-Ala-Ala-Ala-Wang-resin (0.68 g) Got.

4.レジンからの脱保護ペプチドの切り出し
(15)Boc-Ala-Ala-Ala-Ala-Ala-Wang-レジンにTFA/TIS/ H2O(体積比 TFA/TIS/H2O =95/2.5/2.5)(5 mL)を加えて2時間振とうした。
(16)レジンをろ去後、反応液を減圧濃縮して、残渣にIPE (25 mL)を加えて晶析させた。
(17)結晶を減圧ろ過した。
(18)室温で減圧乾燥し、H-Ala-Ala-Ala-Ala-Ala-OH・TFA塩 (60.7 mg) を得た。
4). Cutting out deprotected peptide from resin (15) TFA / TIS / H 2 O (volume ratio TFA / TIS / H 2 O = 95 / 2.5 / 2.5) to Boc-Ala-Ala-Ala-Ala-Ala-Wang-resin ) (5 mL) was added and shaken for 2 hours.
(16) After removing the resin by filtration, the reaction solution was concentrated under reduced pressure, and IPE (25 mL) was added to the residue for crystallization.
(17) The crystals were filtered under reduced pressure.
(18) It dried under reduced pressure at room temperature and obtained H-Ala-Ala-Ala-Ala-Ala-OH * TFA salt (60.7 mg).

〔HPLC分析(実験例9及び比較例6)〕
 実験例9及び比較例6の生成物のアセトニトリル溶液のHPLC分析した結果を表17及び図19及び20に示した。表17は、実験例9及び比較例6の生成物のアセトニトリル溶液のHPLC分析における生成物(ペンタアラニン)の保持時間及び含有率を示す。図19及び20は、それぞれ、実験例9及び比較例6の生成物のアセトニトリル溶液のHPLCクロマトグラムを示す。尚、本HPLC分析は、下記のHPCL条件で分析を行った。
[HPLC analysis (Experimental Example 9 and Comparative Example 6)]
The results of HPLC analysis of acetonitrile solutions of the products of Experimental Example 9 and Comparative Example 6 are shown in Table 17 and FIGS. Table 17 shows the retention time and content of the product (pentaalanine) in the HPLC analysis of the acetonitrile solutions of the products of Experimental Example 9 and Comparative Example 6. 19 and 20 show HPLC chromatograms of acetonitrile solutions of the products of Experimental Example 9 and Comparative Example 6, respectively. This HPLC analysis was performed under the following HPCL conditions.

HPLC条件
カラム:Waters X Bridge
移動相:0.1% TFA水溶液
分析時間:約10分
流速:1 mL/min
検出器:UV 220 nm
HPLC condition column: Waters X Bridge
Mobile phase: 0.1% TFA aqueous solution Analysis time: Approx. 10 minutes Flow rate: 1 mL / min
Detector: UV 220 nm

Figure JPOXMLDOC01-appb-T000023
Figure JPOXMLDOC01-appb-T000023

 上記結果から、本発明の製造方法により高純度の長鎖ペプチドが大量に得られたことが確認できた。 From the above results, it was confirmed that a large amount of highly purified long-chain peptide was obtained by the production method of the present invention.

 本発明の製造方法は、ペプチドの製造に有用である。特に、副反応を抑制して、長鎖ペプチドを大量合成するのに有用である。 The production method of the present invention is useful for the production of peptides. In particular, it is useful for mass synthesis of long-chain peptides while suppressing side reactions.

 1 撹拌用回転体
 5 撹拌機本体
 10 本体
 11 回転駆動軸
 12 吸入口
 13 円筒回転部材
 13A 天板
 13B 底板
 14 吐出口
 16 流通路
 18 接続部
 20 駆動軸
 21 円筒筐体
 22A~22D 放出開口
 23 吸込筒部
 24A~24D 押出突板部
 25A~25D 吸込開口
 30 連通孔
 38 撹拌装置
 40 撹拌用回転体
 41 撹拌用回転体の本体
 41a 撹拌用回転体の本体の略円形状の上面
 41b 撹拌用回転体の本体の略円形状の底面
 41c 撹拌用回転体の本体の外周面である側面
 42 撹拌用回転体の吸入口
 44 撹拌用回転体の吐出口
 46 撹拌用回転体の流通路
 48 接続部
 50 流動抵抗体
 51 流動抵抗体の本体
 51a 流動抵抗体の本体の略円形状の上面
 51b 流動抵抗体の本体の略円形状の底面
 51c 流動抵抗体の本体の外周面である側面
 52 流動抵抗体の吸入口
 54 流動抵抗体の吐出口
 56 流動抵抗体の流通路
 60 駆動軸
 a 回転駆動軸の回転方向
 b 円筒回転部材の回転方向
 d1、d4 外部放出流
 e1~e3 吸込流
 g1~g4、h1~h4 吸込流
 C、L 中心軸線
DESCRIPTION OF SYMBOLS 1 Rotating body for stirring 5 Stirrer main body 10 Main body 11 Rotation drive shaft 12 Suction port 13 Cylindrical rotating member 13A Top plate 13B Bottom plate 14 Discharge port 16 Flow path 18 Connection portion 20 Drive shaft 21 Cylindrical housing 22A-22D Release opening 23 Suction Tube portion 24A to 24D Extrusion protruding plate portion 25A to 25D Suction opening 30 Communication hole 38 Stirrer 40 Stirring rotating body 41 Stirring rotating body main body 41a Stirring rotating body main body 41a A substantially circular upper surface 41b Stirring rotating body 41b A substantially circular bottom surface of the main body 41c A side surface which is the outer peripheral surface of the main body of the stirring rotor 42 A suction port of the stirring rotor 44 A discharge port of the stirring rotor 46 A flow path of the stirring rotor 48 A connection 50 A flow resistance Body 51 Main body of flow resistor 51a Upper surface of substantially circular shape of main body of flow resistor 51b Substantially circular bottom surface of main body of flow resistor 51c Main body of flow resistor Side surface 52 which is an outer peripheral surface 52 Flow resistor suction port 54 Flow resistor discharge port 56 Flow resistor flow path 60 Drive shaft a Rotation drive shaft rotation direction b Cylindrical rotation member rotation direction d1, d4 External discharge flow e1 ~ E3 Suction flow g1 ~ g4, h1 ~ h4 Suction flow C, L Center axis

Claims (5)

 羽根のない遠心式撹拌体の撹拌下に、ペプチドを固相合成することを特徴とするペプチドの製造方法。 A method for producing a peptide, characterized in that the peptide is solid-phase synthesized under stirring of a centrifugal stirring body without blades.  羽根のない遠心式撹拌体が、
 回転軸を中心に回転する本体と、
前記本体の表面に設けられる吸入口と、
前記本体の表面に設けられる吐出口と、
前記吸入口と前記吐出口を繋ぐ流通路と、を備え、
前記吸入口は、前記吐出口よりも前記回転軸に近い位置に配置され、
前記吐出口は、前記吸入口よりも前記回転軸から遠心方向外側の位置に配置されることを特徴とする、撹拌用回転体である、請求項1に記載の製造方法。
A centrifugal stirring body without blades
A main body that rotates about a rotation axis;
An inlet provided on the surface of the body;
A discharge port provided on the surface of the main body;
A flow path connecting the suction port and the discharge port,
The suction port is disposed at a position closer to the rotation shaft than the discharge port,
The manufacturing method according to claim 1, wherein the discharge port is a rotating body for stirring, which is disposed at a position on the outer side in the centrifugal direction from the rotation shaft than the suction port.
 羽根のない遠心式撹拌体の固相法によるペプチド合成のための使用。 Use of a centrifugal stirring body without blades for peptide synthesis by the solid phase method.  羽根のない遠心式撹拌体を搭載したペプチド固相合成用反応容器。 A reaction vessel for peptide solid phase synthesis equipped with a centrifugal stirring body without blades.  グラスフィルターを備えた、請求項4に記載のペプチド固相合成用反応容器。 The reaction vessel for peptide solid phase synthesis according to claim 4, comprising a glass filter.
PCT/JP2018/013147 2017-03-31 2018-03-29 Method for producing peptide Ceased WO2018181679A1 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
KR1020197029768A KR102550717B1 (en) 2017-03-31 2018-03-29 Manufacturing method of peptide
CN201880022224.9A CN110546155B (en) 2017-03-31 2018-03-29 Process for producing peptide
US16/496,245 US11084846B2 (en) 2017-03-31 2018-03-29 Method for producing peptide
EP18775750.5A EP3604323A4 (en) 2017-03-31 2018-03-29 Method for producing peptide
JP2019510112A JP7061606B2 (en) 2017-03-31 2018-03-29 Peptide production method

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2017072780 2017-03-31
JP2017-072780 2017-03-31

Publications (1)

Publication Number Publication Date
WO2018181679A1 true WO2018181679A1 (en) 2018-10-04

Family

ID=63677600

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2018/013147 Ceased WO2018181679A1 (en) 2017-03-31 2018-03-29 Method for producing peptide

Country Status (6)

Country Link
US (1) US11084846B2 (en)
EP (1) EP3604323A4 (en)
JP (1) JP7061606B2 (en)
KR (1) KR102550717B1 (en)
CN (1) CN110546155B (en)
WO (1) WO2018181679A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110483613A (en) * 2019-06-20 2019-11-22 南京知和医药科技有限公司 A kind of industrialization Solid-phase Polypeptide reaction kettle
CN114570266A (en) * 2022-01-14 2022-06-03 中国人民解放军总医院第一医学中心 Medical equipment for platelet rich plasma gel PRG (platelet-rich plasma gel) in-vitro negative pressure cutting treatment

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20250031662A (en) 2023-08-29 2025-03-07 최호윤 Production of peptides using Bacillus and their manufacturing method
KR20250031661A (en) 2023-08-29 2025-03-07 크로마흐 주식회사 Improvement of bacterial recyclability by utilizing in vitro expression characteristics of Bacillus bacteria and industrial biomaterial production process using it
KR20250031663A (en) 2023-08-29 2025-03-07 임진동 Strains for the production of low-carbon feed additives and manufacturing methods using the same
KR20250075842A (en) 2023-11-22 2025-05-29 크로마흐 주식회사 Cellulase production and production method using sequences with high solubility
KR20250075841A (en) 2023-11-22 2025-05-29 크로마흐 주식회사 Method for producing water-soluble EGF peptide using dissolution-inducing sequence
KR20250076858A (en) 2023-11-23 2025-05-30 임진동 Method of utilizing water-soluble base sequences to produce cellulase for feed additives
KR20250076854A (en) 2023-11-23 2025-05-30 최호윤 Method of utilizing special soluble sequences to produce water-soluble EGF
KR20250076855A (en) 2023-11-23 2025-05-30 최호윤 Cellulase production method using water-soluble peptide sequence
KR20250076857A (en) 2023-11-23 2025-05-30 임진동 Base sequence for producing water-soluble EGF and its manufacturing method

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07501261A (en) * 1991-09-04 1995-02-09 ラージ スケール バイオロジー コーポレーション Solid phase application system
JP2000503892A (en) * 1996-01-30 2000-04-04 中外製薬株式会社 Solid phase synthesizer
JP4418019B1 (en) 2009-06-23 2010-02-17 和久 村田 Rotating body for stirring and stirring device
WO2010150656A1 (en) 2009-06-23 2010-12-29 株式会社エディプラス Stirring rotating body and stir device
WO2014046278A1 (en) * 2012-09-21 2014-03-27 株式会社カネカ Protein ligand for affinity isolation matrix
JP2014124540A (en) 2012-12-25 2014-07-07 Unie Flex:Kk Agitating device
JP2015047540A (en) 2013-08-30 2015-03-16 株式会社石井鐵工所 Centrifugal agitator
JP2015136682A (en) * 2014-01-24 2015-07-30 株式会社田定工作所 Rotating body for stirring and stirring device
JP2015171695A (en) 2014-03-12 2015-10-01 ヤマテック株式会社 Agitation device
JP2015535810A (en) * 2012-08-31 2015-12-17 バイオタージ アクチボラゲット Apparatus and method for solid phase synthesis
JP2016117005A (en) 2014-12-19 2016-06-30 富士フイルム株式会社 Liposome producing method and liposome producing device

Family Cites Families (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1031666A (en) * 1912-04-01 1912-07-02 Walter Richmond Centrifugal emulsifier or mixer.
US1645614A (en) * 1926-04-08 1927-10-18 Ormond B Monahan Agitator
US2635860A (en) * 1951-06-11 1953-04-21 Premier Mill Corp Centrifugal mixing device
US2718385A (en) * 1952-12-23 1955-09-20 Ethyl Corp Stirring apparatus
US3170638A (en) * 1963-04-12 1965-02-23 Linwood P Burton Mixing and disintegrating head
US3951741A (en) * 1973-07-10 1976-04-20 Peter Pfaender Process and apparatus for the synthesis of peptides by use of n-carboxyanhydrides
US4138215A (en) * 1976-06-18 1979-02-06 Bodenseewerk Perkin-Elmer & Co., Gmbh Method and apparatus for generating and transferring a gaseous test sample
CA1125995A (en) * 1978-02-21 1982-06-22 Imperial Chemical Industries Limited Chemical process in a medium connected to a rotating body
US4746490A (en) * 1983-09-22 1988-05-24 Saneii Hossain H Solid phase peptide synthesizer
JPH0663945B2 (en) * 1988-08-26 1994-08-22 株式会社日立製作所 Stirrer
US5272075A (en) 1991-09-04 1993-12-21 Large Scale Biology Corporation System for solid phase reactions
US5273656A (en) 1991-09-04 1993-12-28 Large Scale Biology Corporation System for solid phase reactions
DE4239284A1 (en) * 1992-11-23 1994-05-26 Hilti Ag Mixing device for flowable masses
US5744102A (en) 1996-01-30 1998-04-28 Chugai Biopharmaceuticals, Inc. Solid phase synthesizer
JP2001510715A (en) * 1997-07-24 2001-08-07 マグキン、ジェームス、エフ、ジュニア Stationary central tunnel diagnostic catheter with optional separable barrel
US6281331B1 (en) * 1998-03-23 2001-08-28 Trimeris, Inc. Methods and compositions for peptide synthesis
US6857774B2 (en) * 2002-08-02 2005-02-22 Five Star Technologies, Inc. Devices for cavitational mixing and pumping and methods of using same
US20040085856A1 (en) * 2002-10-30 2004-05-06 Murosako James K. Mixer
CN201224725Y (en) * 2008-04-30 2009-04-22 河北科技大学 Novel polypeptide solid phase synthesis apparatus
US20110046349A1 (en) * 2009-07-15 2011-02-24 Matthieu Giraud Process for the production of exenatide and of an exenatide analogue
US20160199798A1 (en) 2012-12-25 2016-07-14 Uniflex Company, Ltd. Mixing capacity measuring device
CN203200209U (en) * 2013-03-29 2013-09-18 申联生物医药(上海)有限公司 Synthesizer temperature control system wide adjustable temperature and synthesizer
CN104311639B (en) * 2014-10-10 2018-02-23 海南中和药业股份有限公司 A kind of synthesis technique of growth hormone release inhibiting hormone
JP6610995B2 (en) 2015-06-24 2019-11-27 エムレボ・ジャパン株式会社 Rotating body for stirring and stirring device

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07501261A (en) * 1991-09-04 1995-02-09 ラージ スケール バイオロジー コーポレーション Solid phase application system
JP2000503892A (en) * 1996-01-30 2000-04-04 中外製薬株式会社 Solid phase synthesizer
JP4418019B1 (en) 2009-06-23 2010-02-17 和久 村田 Rotating body for stirring and stirring device
WO2010150656A1 (en) 2009-06-23 2010-12-29 株式会社エディプラス Stirring rotating body and stir device
JP2015535810A (en) * 2012-08-31 2015-12-17 バイオタージ アクチボラゲット Apparatus and method for solid phase synthesis
WO2014046278A1 (en) * 2012-09-21 2014-03-27 株式会社カネカ Protein ligand for affinity isolation matrix
JP2014124540A (en) 2012-12-25 2014-07-07 Unie Flex:Kk Agitating device
JP2015047540A (en) 2013-08-30 2015-03-16 株式会社石井鐵工所 Centrifugal agitator
JP2015136682A (en) * 2014-01-24 2015-07-30 株式会社田定工作所 Rotating body for stirring and stirring device
JP2015171695A (en) 2014-03-12 2015-10-01 ヤマテック株式会社 Agitation device
JP2016117005A (en) 2014-12-19 2016-06-30 富士フイルム株式会社 Liposome producing method and liposome producing device

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP3604323A4

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110483613A (en) * 2019-06-20 2019-11-22 南京知和医药科技有限公司 A kind of industrialization Solid-phase Polypeptide reaction kettle
CN110483613B (en) * 2019-06-20 2022-05-31 南京知和医药科技有限公司 Industrial polypeptide solid phase reation kettle
CN114570266A (en) * 2022-01-14 2022-06-03 中国人民解放军总医院第一医学中心 Medical equipment for platelet rich plasma gel PRG (platelet-rich plasma gel) in-vitro negative pressure cutting treatment
CN114570266B (en) * 2022-01-14 2023-06-13 中国人民解放军总医院第一医学中心 Medical equipment for in-vitro negative pressure cutting treatment of platelet-rich plasma gel PRG

Also Published As

Publication number Publication date
JP7061606B2 (en) 2022-04-28
KR20190134657A (en) 2019-12-04
KR102550717B1 (en) 2023-06-30
EP3604323A1 (en) 2020-02-05
US11084846B2 (en) 2021-08-10
EP3604323A4 (en) 2021-01-13
US20200024305A1 (en) 2020-01-23
CN110546155A (en) 2019-12-06
JPWO2018181679A1 (en) 2020-02-06
CN110546155B (en) 2023-06-23

Similar Documents

Publication Publication Date Title
JP7061606B2 (en) Peptide production method
CN110294800B (en) Preparation method of somaglutide
CN103864918A (en) Solid-phase synthesis method for liraglutide
CN103224558B (en) A kind of preparation method of Exenatide
CN108341883B (en) Process for producing polypeptide
CN106478805A (en) A kind of preparation method of GLP-1 derivant
CN113880936A (en) Solid-phase synthesis method of abamectin
CN106397573A (en) Solid-phase synthesis method of liraglutide
CN109021092A (en) A kind of synthetic method of Suo Malu peptide
CN114181276A (en) Thioester peptide synthesis method
CN107936094A (en) The synthetic method that a kind of solid liquid phase of Li Laluo peptides is combined
CN103122026A (en) Solid-phase preparation method for exenatide crude product
CN112175067B (en) Preparation method of teduglutide
CN113651875B (en) Oligopeptide-34 synthesis method
CN105367627A (en) Method for preparing terlipressin
CN113801216B (en) Synthesis method of somatostatin
CN115975057A (en) Solid-phase synthesis method of clodotoxin
CN108676086A (en) A kind of synthetic method of Liraglutide
CN111892650A (en) Solid-phase synthesis method of liraglutide
CN114230653A (en) Preparation method of chlorotoxin
CN110964097B (en) Synthesis of exenatide by solid-phase fragment method
CN114805480A (en) Preparation method of octreotide
CN114014925B (en) Somaltulipide main peptide chain and preparation method thereof
CN112679603B (en) Method for preparing teriparatide by solid-liquid phase combination
KR100998175B1 (en) How to prepare somatostatin

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 18775750

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2019510112

Country of ref document: JP

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 20197029768

Country of ref document: KR

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: 2018775750

Country of ref document: EP

ENP Entry into the national phase

Ref document number: 2018775750

Country of ref document: EP

Effective date: 20191031